US3664932A - Objects of aluminum and alloys of aluminum having colored coatings and process - Google Patents

Objects of aluminum and alloys of aluminum having colored coatings and process Download PDF

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Publication number
US3664932A
US3664932A US881846A US3664932DA US3664932A US 3664932 A US3664932 A US 3664932A US 881846 A US881846 A US 881846A US 3664932D A US3664932D A US 3664932DA US 3664932 A US3664932 A US 3664932A
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United States
Prior art keywords
current
dissolution
aluminum
range
colored
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US881846A
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English (en)
Inventor
Jos Patrie
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Cegedur GP
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Cegedur GP
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    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D11/00Electrolytic coating by surface reaction, i.e. forming conversion layers
    • C25D11/02Anodisation
    • C25D11/04Anodisation of aluminium or alloys based thereon
    • C25D11/18After-treatment, e.g. pore-sealing
    • C25D11/20Electrolytic after-treatment
    • C25D11/22Electrolytic after-treatment for colouring layers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B64AIRCRAFT; AVIATION; COSMONAUTICS
    • B64FGROUND OR AIRCRAFT-CARRIER-DECK INSTALLATIONS SPECIALLY ADAPTED FOR USE IN CONNECTION WITH AIRCRAFT; DESIGNING, MANUFACTURING, ASSEMBLING, CLEANING, MAINTAINING OR REPAIRING AIRCRAFT, NOT OTHERWISE PROVIDED FOR; HANDLING, TRANSPORTING, TESTING OR INSPECTING AIRCRAFT COMPONENTS, NOT OTHERWISE PROVIDED FOR
    • B64F1/00Ground or aircraft-carrier-deck installations
    • B64F1/18Visual or acoustic landing aids
    • B64F1/20Arrangement of optical beacons

Definitions

  • ABSTRACT The process for providing colored coatings on aluminum and [30] Foreign Application Priority Data alloys of aluminum in which the surface is first anodized to form a porous layer and colored particles of metal compound DEC. 6, 1968 France are deposited in the porous layer y alternating current elec trolysis with the object mounted as an electrode in an elec- [52] U.S. Cl. ..204/35 N, 294/58 trolyte containing the salt of the metal, and then subjecting the [51 II!!- Cl.
  • the process of this invention comprises restoring, by anodic dissolution, the clear colors observed during the initial stages of deposition, after a dark or black color effect has been obtained on the object formed of aluminum or alloys thereof, due to the presence of metal or metal compound particles in the pores of the formed layer of alumina.
  • anodic dissolution the color turns clear as the treatment progresses and, contrary to what is observed in electrolytic coloring, the color rapidly becomes uniform over the entire surface of the object.
  • the anodic dissolution treatment is highly flexible and thus gives more latitude for regulating the production parameters. This is highly advantageous insofar as commercial operation is concerned.
  • the object is initially anodized, such as in a sulphuric acid bath, to provide the object with a porous layer of alumina.
  • Colored particles of a metal or metal compound are then deposited by electrolysis into the pores of the anodized layer, using a bath containing a dissolved salt of the constituent metal of the particles, giving a dark color effect.
  • the electrolysis is operated with alternating current with the object to be coated forming one of the electrodes, while the other electrode, referred to as the counter-electrode, is made either of the constituent metal of the salt dissolved in the electrolyte or of a material which is resistant to the effect of the bath and which does not give rise to any secondary reactions during the electrolysis, such for example as stainless steel.
  • anodic dissolution in accordance with the practice of this invention.
  • the object to be coated which has a dark color or even a black color due to the presence of an excess of colored particles in the pores of the alumina layer, is mounted as an anode in a continuous current or direct current electrolysis cell. It is believed that the anion of the electrolyte combines with the metal compound deposited in the pores of the alumina layer to form a soluble salt of the metal.
  • Anodic dissolution is accompanied by a lightening and standardization of the color due to the decrease and probably to the standardization of the thickness of the deposit. The operation is terminated by cutting the current when the required color has been obtained.
  • the dissolution stage is carried out in the same bath and in the same cell as the deposition by electrolysis. It is sufficient, for this purpose, to provide a switching device by which it is possible to change from alternating current to direct current. More simply, it is sufficient to provide a diode or a diode bridge in the circuit for converting the alternating current into a rectified unfiltered current which gives the same results as the direct current.
  • the electrolyte comprises an acid solution, and preferably a sulphuric acid solution, of a salt of a metal such as copper,
  • the concentration of metal salts dissolved in the electrolyte may range from 0.15 g/liter to an amount to provide a saturated solution.
  • the operation is carried out at bath temperature within the range of 5-30 C and preferably of about room temperature, either at a constant current density of less than 5 A/dm and preferably at a current density within the range of 0.1 to 2 A/dm or at a constant voltage within the range of 10 to 50 volts and preferably 15 to 25 volts for a period of from 10 seconds to 30 minutes, and generally from A to l5 minutes.
  • the final colored layer can be fixed by any conventional process, such as by sealing in boiling water, varnishing or the like.
  • the color obtained is governed by the nature of the metal and the color intensity is governed both by the current density and by the duration of the anodic dissolution for the same initial color effect. For example, a wide range of reds from pink to deep scarlet, including copper shades, can be obtained with an electrolyte containing copper salts.
  • the salts of nickel, cadmium or cobalt enable browns or gold hues to be obtained.
  • the final appearance is somewhat related to the surface quality of the object before the porous layer of alumina is formed.
  • the color effects obtained by the process are brilliant while on a dull or mat surface, a dull or mat color will be secured.
  • Such surface changes can be effected by conventional or known means including polishing, buffing, glazing, and the like, depending upon the finish required.
  • a mat finish is obtained by cleaning the object for 10 minutes at 50 C in a soda solution having a concentration of 50 g/liter, after which it is washed in a stream of water followed by immersion in nitric acid (36 Be) and then by further rinsing in a stream of water.
  • the glossy or shiny finish is obtained by mechanical polishing or by chemical or electrolytic glossing.
  • EXAMPLE 1 A 99.5 percent pure aluminum sheet is mechanically treated to provide a satin surface and then anodized in a sulphuric acid bath to give a porous surface layer of alumina having a thickness of 15 microns. It is then colored by mounting as an electrode in an electrolysis cell fed with alternating current in which the electrolyte is a sulphuric acid solution of copper sulphate having the following composition:
  • the counter-electrode is made of stainless steel.
  • the cell is then converted to direct current with the sheet mounted as the anode.
  • the sheet is removed after 3 minutes of treatment at 0.2 A/dm at about 20 C.
  • EXAMPLE 2 An aluminum sheet containing 0.6 percent magnesium is chemically treated to provide a shiny finish and then anodized in a sulphuric acid bath to obtain a porous layer of alumina having a thickness of 20 microns. It is then mounted as an electrode in an electrolysis cell fed with alternating current in which the electrolyte is a sulphuric acid solution of copper sulphate having the following composition:
  • a sheet which is black in color is produced after minutes of treatment at 0.6 A/dm THe cell is then fed with rectified direct current (unfiltered) with the sheet mounted as the anode. The sheet is removed after 1 minute and 30 seconds treatment at 0.4 A/dm at C.
  • a sheet which is bright red in color is produced and sealed in boiling water.
  • the color is uniform and brilliant in appearance and resistant to ultra-violet rays and to corrosion.
  • EXAMPLE 3 A section of aluminum alloy containing 0.5% silicon and 0.5% magnesium is mechanically polished and then anodized in a sulphuric bath to provide a surface porous layer of alumina having a thickness of 18 microns. It is then colored by mounting as an electrode in an electrolysis cell fed with alternating current in which the electrolyte is a solution of a mixture of boric acid, nickel sulphate and ammonium sulphate:
  • the counter-electrode is made of nickel.
  • a section which is dark bronze in color is produced after 5 minutes oftreatment at 0.4 A/dm.
  • the section is mounted as the anode and the cell is fed with direct current.
  • the section is removed after 6 minutes oftreatment at 0.1 A/dm at 25 C.
  • the section After sealing in boiling water, the section has a clear, uniform and brilliant bronze colored finish which is resistant to ultra-violet rays and to corrosion.
  • EXAMPLE 4 An aluminum alloy section containing 1% by weight silicon, 1% by weight magnesium and 1% by weight manganese is cleaned with soda and then anodized in a sulphuric bath to obtain a porous surface layer of alumina having a thickness of 12 microns. It is then colored by mounting as an electrode in an electrolysis cell fed with alternating current, in which the electrolyte is a solution of a mixture of boric acid, cobalt sulphate and ammonium sulphate:
  • the counter-electrode is made of stainless steel.
  • the cell is then fed with continuous current or direct cur rent with the section mounted as the anode.
  • the section is removed after 4 minutes oftreatment at 0.2 A/dm at 20 C.
  • the section After scaling in boiling water, the section has a clear, uniform mat bronze color which is resistant to ultra-violet rays and to corrosion.
  • EXAMPLE 5 An aluminum alloy section containing 1% by weight silicon, 1% by weight magnesium and 1% by weight manganese is mechanically polished and then anodized in a sulphuric acid bath to provide a porous surface layer of alumina having a thickness of 15 microns. It is then colored by mounting as an electrode in an electrolysis cell fed with alternating current.
  • the electrolyte is a sulphuric acid solution of copper sulphate:
  • the counter-electrode is made of copper.
  • the cell is then fed with direct current with the section mounted as an anode.
  • the section is removed after 2 minutes of treatment at 20 volts at 20 C.
  • the section After sealing in boiling water, the section has a uniform and brilliant copper red finish which is resistant to ultra-violet rays and to corrosion.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Mechanical Engineering (AREA)
  • Aviation & Aerospace Engineering (AREA)
  • Acoustics & Sound (AREA)
  • Physics & Mathematics (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Application Of Or Painting With Fluid Materials (AREA)
  • Cookers (AREA)
  • Electroplating Methods And Accessories (AREA)
  • Electroplating And Plating Baths Therefor (AREA)
US881846A 1968-12-06 1969-12-03 Objects of aluminum and alloys of aluminum having colored coatings and process Expired - Lifetime US3664932A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR176899 1968-12-06

Publications (1)

Publication Number Publication Date
US3664932A true US3664932A (en) 1972-05-23

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ID=8657921

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US881846A Expired - Lifetime US3664932A (en) 1968-12-06 1969-12-03 Objects of aluminum and alloys of aluminum having colored coatings and process

Country Status (11)

Country Link
US (1) US3664932A (xx)
BE (1) BE742732A (xx)
CA (1) CA979843A (xx)
CH (1) CH503796A (xx)
DE (1) DE1961003B2 (xx)
ES (1) ES374264A1 (xx)
FR (1) FR1596808A (xx)
GB (1) GB1297265A (xx)
LU (1) LU59943A1 (xx)
NL (1) NL6918329A (xx)
SE (1) SE364072B (xx)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3787295A (en) * 1970-04-02 1974-01-22 Alusuisse Method of electrolytic coloring of oxide layers on aluminum and aluminum base alloys
US3878056A (en) * 1973-08-24 1975-04-15 Sumitomo Chemical Co Process for electrolytic coloring of the anodic oxide film on a aluminum or aluminum base alloys
US3892636A (en) * 1972-06-06 1975-07-01 Riken Light Metal Ind Co Method for producing a colored oxide film on an aluminum or aluminum alloy
US3962049A (en) * 1971-05-13 1976-06-08 Kabushiki Kaisha Aiden Process for coloring aluminum anodic oxide film
US4024039A (en) * 1972-08-31 1977-05-17 Honny Chemicals Company, Ltd. Coloring methods for aluminum and aluminum alloys
US4043880A (en) * 1975-07-24 1977-08-23 Sumitomo Aluminum Smelting Co., Ltd. Method for producing green-colored anodic oxide film on aluminum or aluminum base alloy articles
US4310586A (en) * 1978-01-17 1982-01-12 Alcan Research And Development Limited Aluminium articles having anodic oxide coatings and methods of coloring them by means of optical interference effects
US7276293B1 (en) * 2000-05-24 2007-10-02 Fujikura Ltd. Far-infrared radiator and method for producing method

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2197999A1 (en) * 1972-09-05 1974-03-29 Honny Chemicals Co Ltd Electrolytic colouration of aluminium articles - using successively altern-ating and direct current

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3382160A (en) * 1960-03-31 1968-05-07 Asada Tahei Process for inorganically coloring aluminum

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3382160A (en) * 1960-03-31 1968-05-07 Asada Tahei Process for inorganically coloring aluminum

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3787295A (en) * 1970-04-02 1974-01-22 Alusuisse Method of electrolytic coloring of oxide layers on aluminum and aluminum base alloys
US3962049A (en) * 1971-05-13 1976-06-08 Kabushiki Kaisha Aiden Process for coloring aluminum anodic oxide film
US3892636A (en) * 1972-06-06 1975-07-01 Riken Light Metal Ind Co Method for producing a colored oxide film on an aluminum or aluminum alloy
US4024039A (en) * 1972-08-31 1977-05-17 Honny Chemicals Company, Ltd. Coloring methods for aluminum and aluminum alloys
US3878056A (en) * 1973-08-24 1975-04-15 Sumitomo Chemical Co Process for electrolytic coloring of the anodic oxide film on a aluminum or aluminum base alloys
US4043880A (en) * 1975-07-24 1977-08-23 Sumitomo Aluminum Smelting Co., Ltd. Method for producing green-colored anodic oxide film on aluminum or aluminum base alloy articles
US4310586A (en) * 1978-01-17 1982-01-12 Alcan Research And Development Limited Aluminium articles having anodic oxide coatings and methods of coloring them by means of optical interference effects
US7276293B1 (en) * 2000-05-24 2007-10-02 Fujikura Ltd. Far-infrared radiator and method for producing method

Also Published As

Publication number Publication date
ES374264A1 (es) 1972-03-16
NL6918329A (xx) 1970-06-09
LU59943A1 (xx) 1970-06-04
DE1961003A1 (de) 1970-06-18
CA979843A (en) 1975-12-16
BE742732A (xx) 1970-06-05
GB1297265A (xx) 1972-11-22
SE364072B (xx) 1974-02-11
CH503796A (fr) 1971-02-28
FR1596808A (xx) 1970-06-22
DE1961003B2 (de) 1971-09-09

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