US2351605A - Metal treatment - Google Patents

Metal treatment Download PDF

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Publication number
US2351605A
US2351605A US433014A US43301442A US2351605A US 2351605 A US2351605 A US 2351605A US 433014 A US433014 A US 433014A US 43301442 A US43301442 A US 43301442A US 2351605 A US2351605 A US 2351605A
Authority
US
United States
Prior art keywords
nitrite
solution
coating
phosphate
sodium
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
Application number
US433014A
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English (en)
Inventor
Robert C Gibson
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Parker Rust Proof Co
Original Assignee
Parker Rust Proof Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Parker Rust Proof Co filed Critical Parker Rust Proof Co
Priority to US433014A priority Critical patent/US2351605A/en
Application granted granted Critical
Publication of US2351605A publication Critical patent/US2351605A/en
Priority to CH260320D priority patent/CH260320A/fr
Priority to DEP4132A priority patent/DE845135C/de
Priority to AT186083D priority patent/AT186083B/de
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • 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

Definitions

  • This invention relates to the production of phosphate coatings on metal surfaces and relates more particularly to a method of replenishing the solutions which are used for that purpose.
  • the presence of sodium dihydrogen phosphate also has disadvantages.
  • the coating efiiciency of the solution will be impaired by the accumulation of an appreciable amount of sodium phosphate because it increases the solubility of normal zinc phosphate which comprises the bulk of the coating formed on the metal surface.
  • the sodium phosphate will be calculated as a coating material along with zinc phosphate. This will occur whenever the usual titrating methods are employed.
  • the true coating phosphate content of the bath therefore, must be determined by other less convenient means whenever an appreciable amount of sodium phosphate is present.
  • An object of this invention is a method of using a nitrite, such as sodium nitrite, or any similar nitrite which by decomposition in an acid phosphate solution results in a neutralizing action, as an accelerator and at the same time avoid the build up of more than insignificant amounts of the objectionable sodium salt, and at the same time avoid the neutralizing effect which would otherwise be obtained.
  • a nitrite such as sodium nitrite, or any similar nitrite which by decomposition in an acid phosphate solution results in a neutralizing action, as an accelerator and at the same time avoid the build up of more than insignificant amounts of the objectionable sodium salt, and at the same time avoid the neutralizing effect which would otherwise be obtained.
  • Another object is the avoidance of sludge formation and the consequent loss of coating chemicals such as occurs in phosphate solutions when the neutralizing effect of a nitrite is not counteracted.
  • a further object is to enable the operator of a solution to determine by a. simple titration the true coating strength present.
  • a coating dihydrogen phosphate such as zinc phosphate
  • a nitrite such as sodium nitrite
  • an acid with which the nitrite will react with the liberation of nitrous acid and in amount at least equivalent to that required to form a substantially neutral salt by reaction with the nitrite present.
  • the coating metal and the phosphate content of the,replenishing materials be added in substantially the proportions to form zinc dihydrogen phosphate.
  • phoric acid would, of course, result in the presence of sludge, while more than is required would be available to form sodium phosphate.
  • Sodium nitrite being unstable in the presence of acid, must be added separately from the acid phosphate.
  • the nitrite will vary in efliciency within limits, with the rate of production, that is, the greater the amount of surface treated in a given time, the less the amount of nitrite required for a given area coated, because there is less chance for decomposition to occur in the absence of coating formation. It can be seen, therefore, that the amount of acid to be added to combine with the sodium of the sodium nitrite will vary somewhat depending on operating conditions.
  • this factor is compensated for by a more or less corresponding change in consumption of coating chemicals, and .for variations ordinarily encountered the acid may be' incorporated with the coating phosphate material so that the addition of the acid as a separate ingredient is avoided.
  • the acid may be' incorporated with the coating phosphate material so that the addition of the acid as a separate ingredient is avoided.
  • Less phosphate phosmaterial for the purpose of the invention. This may be added along with the acid phosphate as a single mixture.
  • the water in the tank isflrst heated to 110-130 F.
  • processing bath may be prepared by adding in i the proportion of 40 pounds to 100 gallons of water a concentrated solution of the following composition:
  • The' coating solution may be applied to the metal to be coatedby any of the usual methods,
  • the metal for example, fenders, wheels, or other automotive steel parts
  • the other steps incident to this coating operation that is, the necessary cleaning and rinsing operations, are also carried out by the spray method.
  • the metal is carried on a conveyor through a tunnel in which the various steps are performed.
  • a spraying time of approximately one minute in the coating section is usually sufficient to cause a uniform conversion of the steel surface to an insoluble phosphate.
  • the sodium nitrite is preferably added in the same manner.
  • the amount reqired in the solution will vary not only with the rate of production, as has been pointed out, but also to some extent with the ease with which any given kind of steel is coated.
  • the processing time is standardized as it is in the usual spraying installations, it is sometimes necessary to slightly increase the amount of nitrite in order to obtain a satisfactory coating in a given time, since it is impractical to increase the processing time.
  • a range of nitrite, calculated as N02, from .006 to .05% is very satisfactory.
  • the nitrite content of the solution can permanganate in accordance with usual methods.
  • the amount of N02 required varies with the temperature, that is, 006% is satisfactory when operating at around 130 F., while approximately .02-.05% is required at a temperature in the neighborhood of 110 F. 7
  • the amount of nitric acid in the above replenishing formula is sufficient to avoid the formation of sodium dihydrogen phosphate when the higher amounts of nitrite are used and, at the same time, there is insufllcient to cause excessive acidity when only small amounts are employed.
  • nitric acid has been dealt with somewhat in detail. However, it is to be underi stood that other acids may be used in place of it. For example, sulfuric and hydrochloric acid are also capable of counteracting the neutraliz- The nitrite appears to have some catalytic action on the nitrate with the formation of some additional nitrite which also aids in accelerating the coating action.
  • the principle of the invention may be employed in connection with any phosphate solution whose coating action is accelerated by nitrite and is not restricted to instances where ferrous surfaces are coated, since various non-ferrous metals, such as zinc, cadmium, magnesium, copper, and aluminum may also be phosphate coated with the aid of. nitrite.
  • the invention is also applicable to other metallic phosphate solutions; for example, dihydrogen phosphates of manganese, cadmium, and calcium may also be accelerated by a nitrite.

Landscapes

  • 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)
US433014A 1942-03-02 1942-03-02 Metal treatment Expired - Lifetime US2351605A (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
US433014A US2351605A (en) 1942-03-02 1942-03-02 Metal treatment
CH260320D CH260320A (fr) 1942-03-02 1946-08-10 Procédé pour l'obtention d'un revêtement protecteur insoluble sur des surfaces métalliques à l'aide d'une solution phosphatante acide.
DEP4132A DE845135C (de) 1942-03-02 1950-10-01 Verfahren zum Aufbringen von Phosphatueberzuegen auf Metallen
AT186083D AT186083B (de) 1942-03-02 1952-10-11 Verfahren zum Aufbringen von Phosphatüberzügen auf Metallen

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US260320XA 1942-03-02 1942-03-02
US433014A US2351605A (en) 1942-03-02 1942-03-02 Metal treatment

Publications (1)

Publication Number Publication Date
US2351605A true US2351605A (en) 1944-06-20

Family

ID=61187030

Family Applications (1)

Application Number Title Priority Date Filing Date
US433014A Expired - Lifetime US2351605A (en) 1942-03-02 1942-03-02 Metal treatment

Country Status (4)

Country Link
US (1) US2351605A (de)
AT (1) AT186083B (de)
CH (1) CH260320A (de)
DE (1) DE845135C (de)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2540314A (en) * 1947-07-24 1951-02-06 Parker Rust Proof Co Process and compositions for applying phosphate coatings
US2800422A (en) * 1953-04-20 1957-07-23 Piccinelli Achille Process for rust-proofing and passivating iron articles
US2884351A (en) * 1956-01-25 1959-04-28 Parker Rust Proof Co Method of cold rolling ferrous strip stock
US3161549A (en) * 1955-04-08 1964-12-15 Lubrizol Corp Solution for forming zinc phosphate coatings on metallic surfaces
US3939014A (en) * 1974-11-20 1976-02-17 Amchem Products, Inc. Aqueous zinc phosphating solution and method of rapid coating of steel for deforming
US4749417A (en) * 1986-05-12 1988-06-07 The Lea Manufacturing Company Corrosion resistant coating
US4897129A (en) * 1986-05-12 1990-01-30 The Lea Manufacturing Company Corrosion resistant coating

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1153222B (de) * 1956-01-18 1963-08-22 Metallgesellschaft Ag Verfahren zum Aufbringen von Phosphat-ueberzuegen auf Metalloberflaechen und Loesung zur Durchfuehrung des Verfahrens

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2540314A (en) * 1947-07-24 1951-02-06 Parker Rust Proof Co Process and compositions for applying phosphate coatings
US2800422A (en) * 1953-04-20 1957-07-23 Piccinelli Achille Process for rust-proofing and passivating iron articles
US3161549A (en) * 1955-04-08 1964-12-15 Lubrizol Corp Solution for forming zinc phosphate coatings on metallic surfaces
US2884351A (en) * 1956-01-25 1959-04-28 Parker Rust Proof Co Method of cold rolling ferrous strip stock
US3939014A (en) * 1974-11-20 1976-02-17 Amchem Products, Inc. Aqueous zinc phosphating solution and method of rapid coating of steel for deforming
US4749417A (en) * 1986-05-12 1988-06-07 The Lea Manufacturing Company Corrosion resistant coating
US4897129A (en) * 1986-05-12 1990-01-30 The Lea Manufacturing Company Corrosion resistant coating

Also Published As

Publication number Publication date
CH260320A (fr) 1949-03-15
DE845135C (de) 1952-07-28
AT186083B (de) 1956-07-10

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