US3616308A - Method of producing colored coatings on aluminum - Google Patents

Method of producing colored coatings on aluminum Download PDF

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Publication number
US3616308A
US3616308A US773936A US3616308DA US3616308A US 3616308 A US3616308 A US 3616308A US 773936 A US773936 A US 773936A US 3616308D A US3616308D A US 3616308DA US 3616308 A US3616308 A US 3616308A
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United States
Prior art keywords
aluminum
bath
ions
article
alternating current
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US773936A
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English (en)
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William Ernest Cooke
Paul John Sajben
Roy Cowieson Spooner
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Alcan Research and Development Ltd
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Alcan Research and Development Ltd
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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

Definitions

  • ABSTRACT In procedure for producing colored coatings on aluminum by first anodizing the aluminum surface and then treating such anodically coated surface with alternating current in an acidic bath containing metal ions selected from the group consisting of the following cations and anions: Cu, Ag", Pb, and anions consisting of oxygen combined with one of the metals Se, Te and Mn, to produce a colored deposit in the coating, improved coloring results notably in avoiding or inhibiting occurrence oflocalized nonuniformity, especially with darker or more intense tones, are achieved by maintaining a content of aluminum ions in the bath.
  • metal ions selected from the group consisting of the following cations and anions: Cu, Ag", Pb, and anions consisting of oxygen combined with one of the metals Se, Te and Mn
  • the present invention relates to a process for producing colored coatings on aluminum, and more particularly relates to the production of inorganic-colored coatings on aluminum articles.
  • References to aluminum herein will be understood to include aluminum of ordinary commercial purity and aluminum-base alloys that are suitable for conventional anodizing treatments.
  • the term aluminum article as used herein is intended to include semifabricated products, such as rolled aluminum sheet and aluminum extruded sections.
  • the present invention relates to improvements in a previously described two-stage process for producing a colored coating which comprises anodically oxidizing an aluminum article and thereafter treating the anodized article by passing an alternating current between such aluminum article and a counterelectrode, while such aluminum article and electrode are immersed in a bath that contains a dissolved compound of a selected metal in an aqueous acidic medium. Under these circumstances the anodic oxide coating on the aluminum article becomes colored. More particularly, the invention is con cerned with such process wherein the acidic bath of the alternating current treatment contains metal ions selected from the group consisting of the following cations and anions: Cu, Agfl Pb. and anions consisting of oxygen combined with one of the metals Se, Te and Mn. Procedures of this sort are included in the description of U.S. Pat. No. 3,382,160, granted May 7, 1968 to Tahei Asada.
  • the counterelectrode in the alternating current step may be a material, such as graphite (i.e. carbon), which is inert to the electrolyte, or may be formed of other conductive composition, e.g.
  • metal which may advantageously be selected among metals having a solution potential more noble than aluminum in the conventional series of electrode potentials, and which can preferably be the same metal, if available, as constituted by the selected ions in solution in the electrolyte, all as explained in the previous disclosure.
  • a graphite or copper counterelectrode may be effectively employed.
  • a chief object of the present invention is to reduce the incidence of spalling.
  • a further and more specific object is to improve the operation of the above process utilizing metal ions selected from the stated group, notably the second or alternating current treatment stage of such process, so that a full range of tones or shades may be obtained by employing a given bath, including the darker tones that are achieved with higher voltages or longer times or both, while in all cases there is desirable avoidance of deterioration of the colored coating as by spalling or the like.
  • the complete procedure includes first anodizing the aluminum surface to produce the anodic coating thereon, and then subjecting the coated surface to alternating current in an aqueous bath containing the selected metal ions, such bath also containing aluminum ions, as for example in amount represented by at least about I gram per liter of aluminum sulfate (calculated as Al,[SO,],.l8l-l,0), or more generally (and approximately) stated at least about ppm. Al ions.
  • a typical bath may constitute the salt of the metal selected for coloring function, appropriate acidic and related constituents, and an aluminum compound which in dissolved form is in effect an aluminum salt, advantageously containing an anion otherwise present in the electrolyte.
  • a special advantage of the present invention is that a given electrolyte can be employed to provide a wide range of shades or tones, notably up to the darkest values, without difficulty, so that the process has improved flexibility in practice, to accommodate a wide variety of color requirements.
  • a given electrolyte can be employed to provide a wide range of shades or tones, notably up to the darkest values, without difficulty, so that the process has improved flexibility in practice, to accommodate a wide variety of color requirements.
  • the complete process of producing a colored coating on an aluminum surface of an article involves first anodizing the surface in conventional manner to produce an anodic oxide coating, e.g. of a type customarily applied for protective or like purposes.
  • any of a number of known operations may be employed, notably with electrolytes of a group which may be defined as consisting of aqueous solutions of sulfuric acid, chromic acid, or a sulfonic acid such as sulfosalicylic acid, and suitable mixtures of these with other acids or compounds, and while in some cases alternating current anodizing treatment may be feasible, effective results are obtained by anodizing the work with direct current, as for periods of 20 minutes to 60 minutes, in an aqueous solution of sulfuric acid, e.g. 15 percent acid by weight.
  • the operating conditions of the anodizing step do not appear to be very critical, being selected largely to suit the thickness and other characteristics of anodic coating desired; the requirements of the subsequent coloring step are satisfied over a considerable range of thicknesses of porous oxide coating on aluminum,
  • the second step of the process then involves submerging the anodized aluminum article, if desired afier suitable rinsing, in an acidic bath in which a counterelectrode is likewise submerged, such bath comprising an aqueous acidic solution containing the metal selected for coloring function, specifically metal ions selected from the group consisting of the following cations and anions: Cu, Ag Pb, and anions consisting of oxygen combined with one of the metals Se, Te and Mn.
  • alternating current is passed through the solution between the article and the counterelectrode, for sufficient time to effect the desired colored deposit in the oxide coating, e.g. a deposit understood to consist of metal, of the selected ions, which is in chemical combination with oxygen, such as oxide or hydroxide, conveniently herein considered to be oxide.
  • the bath should be a water solution containing the metal ions selected for coloring function, and an acidic constituent, the dissolved compounds being all in relatively low concentration.
  • the bath constituents including nonmetallic anionic constituents, may be variously selected to provide the desired solubility of metal ions and suitable acidity of the electrolyte, and supplemental or further salts and the like may be incorporated, as desired for supplemental purposes that do not interfere with the formation of the colored deposit, or as may result from initial or subsequent pH adjustment.
  • sulfate, borate, acetate, tartrate, phosphate, sulfamate and other common ions have been found appropriate for solutions of one metal or another, e.g.
  • salts of the selected metal or as forming the chosen acidic component will depend on solubility and like requirements of the metal ions, as for example in the case of lead ions, substances such as sulfamic acid and acetic acid and their salts should be utilized instead of sulfate.
  • the metal ions are of anionic nature, compounds appropriately soluble in the acidic bath should be employed, such as alkali metal selenites, selenium oxide, selenic acid, alkali metal tellurites, permanganates, and the like.
  • aluminum is preferably added to the electrolyte in the form of a salt, the anion of which (e.g. sulfate, acetate) is already present in the bath or is otherwise compatible as will be understood or may be readily determined.
  • a presently preferred copper electrolyte contains copper sulfate and sulfuric acid, to which the aluminum may be added as aluminum sulfate.
  • the aluminum can actually be supplied as a soluble form of aluminum .oxide or aluminum hydroxide, then becoming a corresponding dissolved salt in the presence of acidic constituents. Necessary adjustments of acidity for this and other purposes are made by suitable additions such as sulfuric acid, acetic acid, ammonium hydroxide and the like. While some anions, such as halides (except perhaps chlorides in small concentration) are not presently recommended, the essential requirement is to have dissolved aluminum ions present and selection of a suitable and commonly available salt presents no problem in the light of the foregoing.
  • the amount of aluminum present should be sufficient to provide significant inhibition of spalling, i.e. to avoid or materially reduce the occurrence or tendency toward occurrence of minute spots or flaked-off areas, or like spots or defects in the colored product, e.g. in the darker or very dark tones obtainable from the selected metal.
  • spalling is often represented by colorless or pale spots, it may sometimes occur otherwise, as for instance where flaking near the outset of the alternating current treatment leads to a more intense tone due to preferential flow of current to the spalled area.
  • some utility has been noted for lesser amounts, in general, at least about p.p.m.
  • the aluminum compound is added in amount to provide from approximately 1000 to 2500 p.p.m. of al., as for example about 10 to 25 grams per liter of AL ,(SO 1 811,0. Even considerably greater amounts, as up to 40 grams per liter of the aluminum salt (or 4000 ppm. Al), are not believed to be detrimental, so that the upper limit appears primarily economic.
  • the anodized article is then suitably rinsed and submerged in the selected acidic bath which contains the appropriate counterelectrode.
  • the alter nating current is passed, between the article and the electrode, at a conveniently moderate voltage, say from 5 to 20 volts, for a correspondingly appropriate time, e.g. from a few minutes up to 10 or i5 minutes, sometimes with increasing voltage or other suitable electrical control.
  • a conveniently moderate voltage say from 5 to 20 volts
  • a correspondingly appropriate time e.g. from a few minutes up to 10 or i5 minutes, sometimes with increasing voltage or other suitable electrical control.
  • the shade of color achieved depends on the time of treatment and on electrical conditions; for instance, lighter shades are produced by relatively brief treatment with lower voltages, whereas darker or stronger or very dark colors require a longer time or greater electrical values.
  • EXAMPLE 1 Aluminum articles, e.g. aluminum sheets were first anodized as above in the conventional 15 percent sulfuric acid solution for 30 minutes to a film thickness of 0.6 mil, and after rinsing were then subjected to the alternating current treatment, with a counterelectrode of graphite in a copper-containing bath (adjusted to pH about 1.3) having the following composition:
  • the treated articles can preferably be subjected to conventional sealing treatment, as in very hot or boiling water, for usual purposes.
  • sealing treatment as in very hot or boiling water
  • the content of copper salt can be selected over a considerable range, e.g. up to 50 g.p.l., the acid being as required to obtain a preferred pH and the aluminum sulfate being included in amounts, for example, from 2 to 30 g.p.l. or more.
  • EXAMPLE 2 Aluminum sheet was first anodized and then subjected to the alternating treatment as in example 1, except that the bath for the latter contained silver and had the following composition:
  • EXAMPLE 3 Aluminum sheet was first anodized and then subjected to the alternating treatment as in example 1, except that the bath for the latter contained selenium and had the following composition:
  • EXAMPLE 4 Aluminum sheet was first anodized and then subjected to the alternating treatment as in example l, except that the bath for the latter contained tellurium and had the following composition:
  • EXAMPLE 5 In this instance aluminum articles were first anodized by conventional treatment as indicated in other examples, and then subjected to the alternating current treatment, with a graphite counterelectrode, in a bath containing from 25 to 30 g.p.l. oflead acetate, 20 to 25 g.p.l. of acetic acid and 20 g.p.l. of aluminum acetate (Allc l-l o j Alternating current was passed at 13 volts for about 5 minutes. A uniform black coating was produced, whereas similar operation without the aluminum addition tended to exhibit some spalling or like difficulty.
  • step of adding the aluminum compound consists of adding aluminum sulfate to the bath in amount represented by at least about one gram of Al (SO -l8H O per liter.
  • step of adding the aluminum compound consists in adding an aluminum salt to the bath in amount of at least about 2 grams per liter.
  • a method of producing an inorganically colored anodic coating on an aluminum surface ofan article wherein said surface has first been anodized to produce an anodic coating thereon and wherein alternating current is passed between said anodized surface and an electrode while both are immersed in an aqueous acidic bath containing metal ions selected from the group consisting anions consisting of oxygen combined with one of the metals Se, Te and Mn, for producing a colored deposit in the coating
  • the procedure comprising adding to said bath an aluminum compound in an amount to provide in solution in said bath at least about 200 p.p.m. of aluminum ions and effecting said alternating current treatment while maintaining aluminum ions in said bath in amount of at least about 200 p.p.m.
  • a method as defined in claim 10, which comprises adding Al,(SO 'l8I-i O to the bath in amount of at least about l0 grams per liter to provide said aluminum ions.
  • a method as defined in claim 7, which includes the step of first anodizing said aluminum surface of the article with direct current between said article as anode and a cathode in an aqueous solution of sulfuric acid to produce said anodic coating.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)
  • Chemical Treatment Of Metals (AREA)
  • Electroplating And Plating Baths Therefor (AREA)
  • Cosmetics (AREA)
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US773936A 1967-11-24 1968-11-06 Method of producing colored coatings on aluminum Expired - Lifetime US3616308A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB53699/67A GB1241296A (en) 1967-11-24 1967-11-24 Process for colouring anodised aluminium by electrolytic deposition
GB5369867 1967-11-24

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US3616308A true US3616308A (en) 1971-10-26

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AT (1) AT305721B (OSRAM)
BE (1) BE724327A (OSRAM)
CH (1) CH495431A (OSRAM)
DE (1) DE1809741C3 (OSRAM)
DK (1) DK131794C (OSRAM)
ES (1) ES360607A1 (OSRAM)
FI (1) FI47115C (OSRAM)
FR (1) FR1592472A (OSRAM)
GB (1) GB1241296A (OSRAM)
IE (1) IE32543B1 (OSRAM)
IL (1) IL31135A (OSRAM)
LU (1) LU57373A1 (OSRAM)
NL (1) NL141579B (OSRAM)
NO (1) NO120098B (OSRAM)
SE (1) SE337972B (OSRAM)
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3772166A (en) * 1972-07-21 1973-11-13 Perma Technological Ind Inc Electrolytic process for slating a curvilinear aluminum workpiece
US3912602A (en) * 1973-11-09 1975-10-14 Alusuisse Process for colouring aluminum electrolytically

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2219437B1 (OSRAM) * 1973-02-23 1975-08-22 Pechiney Aluminium
US4177299A (en) * 1978-01-27 1979-12-04 Swiss Aluminium Ltd. Aluminum or aluminum alloy article and process
US4431489A (en) * 1983-03-31 1984-02-14 Kaiser Aluminum & Chemical Corporation Coloring process for anodized aluminum products
US4931151A (en) * 1989-04-11 1990-06-05 Novamax Technologies Holdings Inc. Method for two step electrolytic coloring of anodized aluminum
US8050831B2 (en) 2006-04-07 2011-11-01 Ford Global Technologies, Llc Vehicle engine speed control for a continuously variable transmission
WO2010039937A1 (en) * 2008-10-01 2010-04-08 Lorin Industries Outdoor-suitable antique copper color aluminum material and process
JP5908266B2 (ja) * 2011-11-30 2016-04-26 株式会社Screenホールディングス 陽極化成装置及びそれを備えた陽極化成システム並びに半導体ウエハ
US20130153427A1 (en) * 2011-12-20 2013-06-20 Apple Inc. Metal Surface and Process for Treating a Metal Surface
CN107190299B (zh) * 2017-06-14 2023-07-04 江苏昊科汽车空调有限公司 用于空调压缩机旋转压缩盘铝合金的硬质氧化方法

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3772166A (en) * 1972-07-21 1973-11-13 Perma Technological Ind Inc Electrolytic process for slating a curvilinear aluminum workpiece
US3912602A (en) * 1973-11-09 1975-10-14 Alusuisse Process for colouring aluminum electrolytically

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NL141579B (nl) 1974-03-15
NO120098B (OSRAM) 1970-08-24
LU57373A1 (OSRAM) 1969-03-03
DK131794C (da) 1976-02-02
DE1809741B2 (OSRAM) 1971-02-04
IE32543B1 (en) 1973-09-05
BE724327A (OSRAM) 1969-05-22
US3616309A (en) 1971-10-26
AT305721B (de) 1973-03-12
FI47115C (fi) 1973-09-10
IL31135A (en) 1972-10-29
IL31135A0 (en) 1969-01-29
ES360607A1 (es) 1970-07-16
IE32543L (en) 1969-05-24
CH495431A (fr) 1970-08-31
DE1809741A1 (de) 1969-11-06
FR1592472A (OSRAM) 1970-05-11
SE337972B (OSRAM) 1971-08-23
YU34438B (en) 1979-07-10
GB1241296A (en) 1971-08-04
DE1809741C3 (de) 1975-10-23
DK131794B (da) 1975-09-01
NL6816721A (OSRAM) 1969-05-28
FI47115B (OSRAM) 1973-05-31
YU273068A (en) 1978-12-31

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