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US20020157961A1 - Anodizing process, with low environmental impact, for a woodpiece of aluminum or aluminum alloys - Google Patents

Anodizing process, with low environmental impact, for a woodpiece of aluminum or aluminum alloys Download PDF

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Publication number
US20020157961A1
US20020157961A1 US10/078,693 US7869302A US2002157961A1 US 20020157961 A1 US20020157961 A1 US 20020157961A1 US 7869302 A US7869302 A US 7869302A US 2002157961 A1 US2002157961 A1 US 2002157961A1
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Prior art keywords
workpiece
process according
aluminum
anodizing
acid
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Abandoned
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US10/078,693
Inventor
Alessandro Dattilo
Salvatore Tamiro
Carlo Romano
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Alenia Aermacchi SpA
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Alenia Aeronautica SpA
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Assigned to ALENIA AERONAUTICA S.P.A. reassignment ALENIA AERONAUTICA S.P.A. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: DATTILO, ALESSANDRO, ROMANO, CARLO, TAMIRO, SALVATORE
Publication of US20020157961A1 publication Critical patent/US20020157961A1/en
Abandoned legal-status Critical Current

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D11/00—Electrolytic coating by surface reaction, i.e. forming conversion layers
    • C25D11/02—Anodisation
    • C25D11/04—Anodisation of aluminium or alloys based thereon
    • C25D11/06—Anodisation of aluminium or alloys based thereon characterised by the electrolytes used

Definitions

  • the present invention relates to an anodizing process for a workpiece (such as, for example, a part or a component of a system) of aluminium or aluminium alloys, this definition being intended to comprise pure or almost pure aluminium, as well as combinations thereof in all percentages with other elements.
  • a workpiece such as, for example, a part or a component of a system
  • aluminium or aluminium alloys this definition being intended to comprise pure or almost pure aluminium, as well as combinations thereof in all percentages with other elements.
  • this process makes use of the above-mentioned workpiece as the anode of an electrolytic cell in the presence of an aqueous acid solution in order to form on the surface of the workpiece a coating of aluminium oxide.
  • This coating results in better properties concerning the resistance to corrosion and the adhesion of paints, bonding agents and other organic coatings suitable for improving the appearance or the resistance to corrosion of the finished workpiece.
  • this acid solution substantially comprises sulphuric acid at high concentrations or chromic acid, the latter being the compound mainly used in the field of aeronautics.
  • the problem addressed by the present invention is to provide an anodizing process having a lesser toxicological impact on the environment in comparison with the known types, avoiding the use of chromic acid whilst nevertheless obtaining anodized workpieces having properties which are at least equivalent to those of workpieces obtained by conventional means.
  • the process according to the invention has the advantage of eliminating, or in any case greatly reducing, the production of industrial waste, in particular waste containing compounds of chromium, without causing the formation of other waste materials having particular toxic or dangerous properties.
  • the process according to the invention further has the advantage of having a cycle time which is approximately 40% short of that of the analogous process which makes use of chromic acid, producing anodized workpieces having properties at least equivalent if not superior. Consequently, the process according to the invention allows a considerable reduction in running costs to be obtained in that it results in lower costs for the treatment of the waste and involves a substantially lower rate of consumption for the different chemicals used for replenishing the baths, which have an operational life greater than those used in known processes.
  • the aqueous acid solution of the process according to the invention preferably contains from 20 to 80 g sulphuric acid and from 30 to 120 g L(+)-tartaric acid per liter of solution.
  • the aqueous solution is maintained, during the anodizing treatment, at a temperature of between ambient temperature and 120° C. and, more preferably, between 25 and 35° C.
  • the electrolytic cell in which the process according to the invention is carried out, is preferably subjected to a voltage of between 1 and 120 V and, more preferably, of between 10 and 30 V.
  • the process according to the invention advantageously has a duration of between 5 and 120 minutes and, preferably, of between 5 and 30 minutes.
  • the anodizing process is generally preceded by a cleaning and/or deoxidizing treatment of the workpiece to be anodized and can be followed by a sealing treatment and, optionally, rinsing for the anodized workpiece.
  • these treatments are of conventional type and completely compatible with the present invention and can be selected at will from treatments known to this end by the person skilled in the art.
  • the workpiece advantageously has, upon completion of the anodizing treatment, an oxidized surface coating having a thickness of between a few micrometers and several tens of micrometers.
  • a workpiece (of a 2000-series aluminium alloy having dimensions of 150 ⁇ 100 ⁇ 1 mm) was first subjected in a conventional manner to cleaning and deoxidizing treatments, such as de- greasing by immersion for approximately 10 minutes, rinsing by immersion in drinking water for approximately 3 minutes, pickling/deoxidation by immersion for approximately 10 minutes and rinsing by immersion in drinking water, preferably followed by further rinsing by immersion in deionized water for a total of approximately 3 minutes.
  • cleaning and deoxidizing treatments such as de- greasing by immersion for approximately 10 minutes, rinsing by immersion in drinking water for approximately 3 minutes, pickling/deoxidation by immersion for approximately 10 minutes and rinsing by immersion in drinking water, preferably followed by further rinsing by immersion in deionized water for a total of approximately 3 minutes.
  • the workpiece was then used as the anode of an electrochemical cell, in which the cathode was constituted by corrosion-resistant steel of the type AISI 321 and having a surface area equal to or greater than that to be oxidized and in the presence of an aqueous acid solution containing 45 g sulphuric acid and 80 g L(+)-tartaric acid per liter of solution and was maintained at a temperature of between 30 and 35° C. The workpiece was kept completely immersed in the acid solution.
  • the electrical voltage was increased from an initial value of 0 V to a value of 18 V at a rate in the order of 3.6 V/min.
  • the final voltage value was maintained for 25 minutes, producing on the workpiece, upon completion of the anodizing treatment, an oxidized coating having a thickness of approximately 5 ⁇ m.
  • the anodized workpiece was then subjected to treatments which are conventional per se, such as rinsing with drinking water, preferably followed by further rinsing with deionized water for an overall immersion time of approximately 3 minutes and sealing by immersion for approximately 45 minutes.
  • treatments which are conventional per se, such as rinsing with drinking water, preferably followed by further rinsing with deionized water for an overall immersion time of approximately 3 minutes and sealing by immersion for approximately 45 minutes.
  • the workpiece was then dried with air, in particular at a low temperature, if good properties of adhesiveness were required for the oxide.
  • a workpiece (of a 7000-series aluminium alloy having dimensions of 150 ⁇ 100 ⁇ 1 mm) was first subjected in a conventional manner to cleaning and deoxidizing treatments, similar to those described with reference to Example 1.
  • the workpiece was then used as the anode of an electrochemical cell, in which the cathode was constituted by corrosion-resistant steel of the type AISI 321 and having a surface area equal to or greater than that to be oxidized and in the presence of an aqueous acid solution containing 45 g sulphuric acid and 80 g L(+)-tartaric acid per liter of solution and was maintained at a temperature of between 30 and 35° C. The workpiece was kept completely immersed in the acid solution.
  • the electrical voltage was increased from an initial value of 0 V to a value of 15 V at a rate in the order of 3 V/min.
  • the final voltage value was maintained for 25 minutes, producing on the workpiece, upon completion of the anodizing treatment, an oxidized coating having a thickness of approximately 5 ⁇ m.
  • a workpiece (of a plated aluminium alloy or pure aluminium having dimensions of 150 ⁇ 100 ⁇ 1 mm) was first subjected, in a conventional manner, to cleaning and deoxidizing treatments, similar to those described with reference to Example 1.
  • the workpiece was then used as the anode of an electrochemical cell, in which the cathode was constituted by corrosion-resistant steel of the type AISI 321 and having a surface area equal to or greater than that to be oxidized and in the presence of an aqueous acid solution containing 45 g sulphuric acid and 80 g L(+)-tartaric acid per liter of solution and was maintained at a temperature of between 30 and 35° C. The workpiece was kept completely immersed in the acid solution.
  • the electrical voltage was increased from an initial value of 0 V to a value of 15 V at a rate in the order of 3 V/min.
  • the final voltage value was maintained for 25 minutes, producing on the workpiece, upon completion of the anodizing treatment, an oxidized coating having a thickness of approximately 5 ⁇ m.
  • a workpiece (of a plated aluminium alloy or a pure aluminium having dimensions of 150 ⁇ 100 ⁇ 1 mm) was first subjected in a conventional manner to cleaning and deoxidizing treatments, similar to those described with reference to Example 1.
  • the workpiece was then used as the anode of an electrochemical cell, in which the cathode was constituted by corrosion-resistant steel of the type AISI 321 and having a surface area equal to or greater than that to be oxidized and in the presence of an aqueous acid solution containing 65 g chromic acid and was maintained at a temperature of between 35 and 40° C.
  • the workpiece was kept completely immersed in the acid solution.
  • the electrical voltage was increased from an initial value of 0 V to a value of 40 V at a rate in the order of 5 V/min.
  • the final voltage value was maintained for 45 minutes, producing on the workpiece, upon completion of the anodizing treatment, an oxidized coating having a thickness of approximately 3 ⁇ m.
  • aqueous acid solution could contain, in addition to sulphuric acid and tartaric acid, any other components or combinations of components which are compatible with those substances.

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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)
  • Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
  • Catalysts (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)

Abstract

The process for anodizing a workpiece of aluminum or aluminum alloys provides for the use of the workpiece as the anode of an electrolytic cell in the presence of an aqueous acid solution which contains from 10 to 200 g sulfuric acid and from 5 to 200 g L(+)-tartaric acid.

Description

    DESCRIPTION
  • The present invention relates to an anodizing process for a workpiece (such as, for example, a part or a component of a system) of aluminium or aluminium alloys, this definition being intended to comprise pure or almost pure aluminium, as well as combinations thereof in all percentages with other elements. [0001]
  • In greater detail, this process makes use of the above-mentioned workpiece as the anode of an electrolytic cell in the presence of an aqueous acid solution in order to form on the surface of the workpiece a coating of aluminium oxide. [0002]
  • This coating results in better properties concerning the resistance to corrosion and the adhesion of paints, bonding agents and other organic coatings suitable for improving the appearance or the resistance to corrosion of the finished workpiece. [0003]
  • Conventionally, this acid solution substantially comprises sulphuric acid at high concentrations or chromic acid, the latter being the compound mainly used in the field of aeronautics. [0004]
  • The problem addressed by the present invention is to provide an anodizing process having a lesser toxicological impact on the environment in comparison with the known types, avoiding the use of chromic acid whilst nevertheless obtaining anodized workpieces having properties which are at least equivalent to those of workpieces obtained by conventional means. [0005]
  • This problem is solved according to the invention by an anodizing process of the type indicated in the introduction to the present description and characterized in that the aqueous acid solution contains from 10 to 200 g sulphuric acid and from 5 to 200 g L(+)-tartaric acid per liter of solution. [0006]
  • The process according to the invention has the advantage of eliminating, or in any case greatly reducing, the production of industrial waste, in particular waste containing compounds of chromium, without causing the formation of other waste materials having particular toxic or dangerous properties. [0007]
  • The process according to the invention further has the advantage of having a cycle time which is approximately 40% short of that of the analogous process which makes use of chromic acid, producing anodized workpieces having properties at least equivalent if not superior. Consequently, the process according to the invention allows a considerable reduction in running costs to be obtained in that it results in lower costs for the treatment of the waste and involves a substantially lower rate of consumption for the different chemicals used for replenishing the baths, which have an operational life greater than those used in known processes. [0008]
  • The aqueous acid solution of the process according to the invention preferably contains from 20 to 80 g sulphuric acid and from 30 to 120 g L(+)-tartaric acid per liter of solution. [0009]
  • Again preferably, the aqueous solution is maintained, during the anodizing treatment, at a temperature of between ambient temperature and 120° C. and, more preferably, between 25 and 35° C. [0010]
  • The electrolytic cell, in which the process according to the invention is carried out, is preferably subjected to a voltage of between 1 and 120 V and, more preferably, of between 10 and 30 V. [0011]
  • The process according to the invention advantageously has a duration of between 5 and 120 minutes and, preferably, of between 5 and 30 minutes. [0012]
  • The anodizing process is generally preceded by a cleaning and/or deoxidizing treatment of the workpiece to be anodized and can be followed by a sealing treatment and, optionally, rinsing for the anodized workpiece. In principle, these treatments are of conventional type and completely compatible with the present invention and can be selected at will from treatments known to this end by the person skilled in the art. [0013]
  • The workpiece advantageously has, upon completion of the anodizing treatment, an oxidized surface coating having a thickness of between a few micrometers and several tens of micrometers. [0014]
  • There now follow, merely by way of non-limiting, illustrative example, examples of the anodizing process according to the invention, as well as a comparative example performed by conventional techniques.[0015]
    • EXAMPLE 1
  • Anodizing a 2000-Series Aluminium Alloy with Sulphuric-Tartaric Acid [0016]
  • A workpiece (of a 2000-series aluminium alloy having dimensions of 150×100×1 mm) was first subjected in a conventional manner to cleaning and deoxidizing treatments, such as de- greasing by immersion for approximately 10 minutes, rinsing by immersion in drinking water for approximately 3 minutes, pickling/deoxidation by immersion for approximately 10 minutes and rinsing by immersion in drinking water, preferably followed by further rinsing by immersion in deionized water for a total of approximately 3 minutes. [0017]
  • The workpiece was then used as the anode of an electrochemical cell, in which the cathode was constituted by corrosion-resistant steel of the type AISI 321 and having a surface area equal to or greater than that to be oxidized and in the presence of an aqueous acid solution containing 45 g sulphuric acid and 80 g L(+)-tartaric acid per liter of solution and was maintained at a temperature of between 30 and 35° C. The workpiece was kept completely immersed in the acid solution. [0018]
  • The electrical voltage was increased from an initial value of 0 V to a value of 18 V at a rate in the order of 3.6 V/min. The final voltage value was maintained for 25 minutes, producing on the workpiece, upon completion of the anodizing treatment, an oxidized coating having a thickness of approximately 5 μm. [0019]
  • The anodized workpiece was then subjected to treatments which are conventional per se, such as rinsing with drinking water, preferably followed by further rinsing with deionized water for an overall immersion time of approximately 3 minutes and sealing by immersion for approximately 45 minutes. The workpiece was then dried with air, in particular at a low temperature, if good properties of adhesiveness were required for the oxide. [0020]
  • The properties of this oxide are indicated in Table I. [0021]
    • EXAMPLE 2 Anodizing a 7000-Series Aluminium Alloy with Sulphuric-Tartaric Acid
  • A workpiece (of a 7000-series aluminium alloy having dimensions of 150×100×1 mm) was first subjected in a conventional manner to cleaning and deoxidizing treatments, similar to those described with reference to Example 1. [0022]
  • The workpiece was then used as the anode of an electrochemical cell, in which the cathode was constituted by corrosion-resistant steel of the type AISI 321 and having a surface area equal to or greater than that to be oxidized and in the presence of an aqueous acid solution containing 45 g sulphuric acid and 80 g L(+)-tartaric acid per liter of solution and was maintained at a temperature of between 30 and 35° C. The workpiece was kept completely immersed in the acid solution. [0023]
  • The electrical voltage was increased from an initial value of 0 V to a value of 15 V at a rate in the order of 3 V/min. The final voltage value was maintained for 25 minutes, producing on the workpiece, upon completion of the anodizing treatment, an oxidized coating having a thickness of approximately 5 μm. [0024]
  • The anodized workpiece was then subjected to rinsing and sealing treatments, which are conventional per se, similar to those described with reference to Example 1. [0025]
  • The properties of the oxide coating obtained are indicated in Table I. [0026]
    • EXAMPLE 3 Anodizing Plated or Pure Aluminium with Sulphuric-Tartaric Acid
  • A workpiece (of a plated aluminium alloy or pure aluminium having dimensions of 150×100×1 mm) was first subjected, in a conventional manner, to cleaning and deoxidizing treatments, similar to those described with reference to Example 1. [0027]
  • The workpiece was then used as the anode of an electrochemical cell, in which the cathode was constituted by corrosion-resistant steel of the type AISI 321 and having a surface area equal to or greater than that to be oxidized and in the presence of an aqueous acid solution containing 45 g sulphuric acid and 80 g L(+)-tartaric acid per liter of solution and was maintained at a temperature of between 30 and 35° C. The workpiece was kept completely immersed in the acid solution. [0028]
  • The electrical voltage was increased from an initial value of 0 V to a value of 15 V at a rate in the order of 3 V/min. The final voltage value was maintained for 25 minutes, producing on the workpiece, upon completion of the anodizing treatment, an oxidized coating having a thickness of approximately 5 μm. [0029]
  • The anodized workpiece was then subjected to rinsing and sealing treatments, which are conventional per se, similar to those described with reference to Example 1. [0030]
  • The properties of the oxide coating obtained are indicated in Table I. [0031]
    • EXAMPLE 4 (FOR COMPARATIVE PURPOSES) Anodizing with Chromic Acid
  • A workpiece (of a plated aluminium alloy or a pure aluminium having dimensions of 150×100×1 mm) was first subjected in a conventional manner to cleaning and deoxidizing treatments, similar to those described with reference to Example 1. [0032]
  • The workpiece was then used as the anode of an electrochemical cell, in which the cathode was constituted by corrosion-resistant steel of the type AISI 321 and having a surface area equal to or greater than that to be oxidized and in the presence of an aqueous acid solution containing 65 g chromic acid and was maintained at a temperature of between 35 and 40° C. The workpiece was kept completely immersed in the acid solution. [0033]
  • The electrical voltage was increased from an initial value of 0 V to a value of 40 V at a rate in the order of 5 V/min. The final voltage value was maintained for 45 minutes, producing on the workpiece, upon completion of the anodizing treatment, an oxidized coating having a thickness of approximately 3 μm. [0034]
  • The anodized workpiece was then subjected to rinsing and sealing treatments, which are conventional per se, similar to those described with reference to Example 1. [0035]
  • The properties of the oxide coating obtained are indicated in Table I. [0036]
    TABLE I
    Prior art
    Chromic acid Prior art INVENTION
    Property Test method (Example 4) Sulphuric acid (Examples 1, 2, 3)
    Weight of oxide ASTM B 137 >32 mg/dm2 >32 mg/dm2 >40 mg/dm2
    Corrosion resistance Tests in saline mist ac- No corrosion points after No corrosion points after No corrosion points after
    cording to Iso 7253 exposure for 500 hours exposure for 500 hours exposure for 750 hours
    Impact test according to No detachment of paint or
    ASTM D 2794 only slight cracking of paint NOT APPLICABLE No detachment of paint
    Paint adhesion Adhesion without condi-
    tioning according to ISO 100% adhesion 90% adhesion 100% adhesion
    2409
    Adhesion after condition-
    ing in water for 14 days 100% adhesion 80% adhesion 100% adhesion
    according to ISO 2409
    Influence of oxide on Fatigue tests on cylindrical Reduction in fatigue cycles Reduction in fatigue cy-
    fatigue life of base test pieces at frequency of not greater than 25% Unsatisfactory cles not greater than 15%
    metal 10-140 Hz, ratio R:0.1
  • A comparison of the results of the tests carried out on the workpieces of the Examples according to the invention and the Example for comparative purposes establishes that the process according to the invention produces oxides having properties which are superior to those of the oxides obtained with conventional processes. Furthermore, the process according to the invention offers environmental advantages associated with the different types of product used, and has a duration which is substantially shorter. [0037]
  • Of course, without altering the principle of the invention, the details of implementation and the embodiments can vary extensively in relation to the description, which is given purely by way of example, without in any way departing from the scope thereof. In particular, the aqueous acid solution could contain, in addition to sulphuric acid and tartaric acid, any other components or combinations of components which are compatible with those substances. [0038]

Claims (7)

What is claimed is:
1. Process for anodizing a workpiece of aluminium or aluminium alloys, which provides for the use of the workpiece as the anode of an electrolytic cell in the presence of an aqueous acid solution,
wherein the aqueous acid solution contains from 10 to 200 g sulphuric acid and from 5 to 200 g L(+)-tartaric acid.
2. Process according to claim 1, wherein the aqueous acid solution contains from 20 to 80 g sulphuric acid and from 30 to 120 g L(+)-tartaric acid per liter of solution.
3. Process according to either of the preceding claims, wherein the solution is maintained, during the anodizing treatment, at a temperature of between ambient temperature and 120° C., and preferably between 25 and 35° C.
4. Process according to claim 1, wherein the electrolytic cell is subjected to a voltage of between 1 and 120 V, and preferably of between 10 and 30 V.
5. Process according to claim 1, wherein it has a duration of between 5 and 120 minutes, and preferably of between 5 and 30 minutes.
6. Process according to claim 1, wherein it is preceded by a cleaning, deoxidizing and rinsing treatment for the workpiece to be anodized.
7. Process according to claim 1, wherein it is followed by a rinsing and sealing treatment for the anodized workpiece.
US10/078,693 2001-02-20 2002-02-19 Anodizing process, with low environmental impact, for a woodpiece of aluminum or aluminum alloys Abandoned US20020157961A1 (en)

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ITTO2001A000149 2001-02-20
IT2001TO000149A ITTO20010149A1 (en) 2001-02-20 2001-02-20 LOW ECOLOGICAL ANODIZATION PROCEDURE OF A PIECE OF ALUMINUM OR ALUMINUM ALLOYS.

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Cited By (11)

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Publication number Priority date Publication date Assignee Title
US20040050709A1 (en) * 2002-09-17 2004-03-18 The Boeing Company Accelerated sulfuric acid and boric sulfuric acid anodize process
US20070092739A1 (en) * 2005-10-25 2007-04-26 Steele Leslie S Treated Aluminum article and method for making same
US20070267299A1 (en) * 2003-01-30 2007-11-22 Yoshiyuki Mitani Method for Forming Anodic Oxide Layer on Surface of Aluminum or Aluminum Alloy
US20090107848A1 (en) * 2007-10-29 2009-04-30 Pilar Ocon Esteban Procedure for anodising aluminium or aluminium alloys
US20110120873A1 (en) * 2008-02-08 2011-05-26 Airbus Operations Gmbh Multifunctional coating of aluminium pieces
US20140008236A1 (en) * 2012-07-04 2014-01-09 Universite De Lorraine Anodization treatment method for aluminum alloys containing cooper
US20160102417A1 (en) * 2014-10-13 2016-04-14 United Technologies Corporation Hierarchically structured duplex anodized aluminum alloy
WO2016116949A1 (en) 2015-01-19 2016-07-28 Council Of Scientific & Industrial Research A process for the preparation of corrosion resistant sealed anodized coatings on aluminum alloy
CN110735169A (en) * 2018-07-18 2020-01-31 列奥纳多股份公司 Anodizing method for corrosion protection of aluminum or aluminum alloy elements used in aircraft structures
CN119800467A (en) * 2025-03-13 2025-04-11 安徽木易科技有限公司 Method and device for multicolor micro-arc oxidation of alloy surface
US12385155B2 (en) 2022-04-29 2025-08-12 Airbus Operations Gmbh Methods for anodizing a part surface and subsequently coating the anodized part surface for corrosion protection purposes

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FR2838754B1 (en) * 2002-04-22 2005-03-18 Messier Bugatti METHOD FOR ANODIZING AN ALUMINUM ALLOY PIECE
DE10361888B3 (en) * 2003-12-23 2005-09-22 Airbus Deutschland Gmbh Anodizing process for aluminum materials
DE102004021926A1 (en) 2004-05-04 2005-12-01 Mtu Aero Engines Gmbh A method of making a coating and anode for use in such a method
CN111112943B (en) * 2018-10-31 2022-04-15 江苏瑞尔隆鼎实业有限公司 Method for machining ABS/ESC valve body for automobile braking system

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Cited By (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20040050709A1 (en) * 2002-09-17 2004-03-18 The Boeing Company Accelerated sulfuric acid and boric sulfuric acid anodize process
US20070267299A1 (en) * 2003-01-30 2007-11-22 Yoshiyuki Mitani Method for Forming Anodic Oxide Layer on Surface of Aluminum or Aluminum Alloy
US20070092739A1 (en) * 2005-10-25 2007-04-26 Steele Leslie S Treated Aluminum article and method for making same
US7527872B2 (en) 2005-10-25 2009-05-05 Goodrich Corporation Treated aluminum article and method for making same
US20090107848A1 (en) * 2007-10-29 2009-04-30 Pilar Ocon Esteban Procedure for anodising aluminium or aluminium alloys
EP2055810A2 (en) * 2007-10-29 2009-05-06 Airbus Espana, S.L. Procedure for anodising aluminium or aluminium alloys
US9334577B2 (en) * 2008-02-08 2016-05-10 Airbus Operations Gmbh Multifunctional coating of aluminium pieces
US20110120873A1 (en) * 2008-02-08 2011-05-26 Airbus Operations Gmbh Multifunctional coating of aluminium pieces
US20140008236A1 (en) * 2012-07-04 2014-01-09 Universite De Lorraine Anodization treatment method for aluminum alloys containing cooper
US20160102417A1 (en) * 2014-10-13 2016-04-14 United Technologies Corporation Hierarchically structured duplex anodized aluminum alloy
US10094037B2 (en) * 2014-10-13 2018-10-09 United Technologies Corporation Hierarchically structured duplex anodized aluminum alloy
US10793966B2 (en) 2014-10-13 2020-10-06 Raytheon Technologies Corporation Hierarchically structured duplex anodized aluminum alloy
US11299815B2 (en) 2014-10-13 2022-04-12 Raytheon Technologies Corporation Hierarchically structured duplex anodized aluminum alloy
WO2016116949A1 (en) 2015-01-19 2016-07-28 Council Of Scientific & Industrial Research A process for the preparation of corrosion resistant sealed anodized coatings on aluminum alloy
US10920332B2 (en) * 2015-01-19 2021-02-16 Council Of Scientific And Industrial Research Process for the preparation of corrosion resistance sealed anodized coatings on aluminum alloy
CN110735169A (en) * 2018-07-18 2020-01-31 列奥纳多股份公司 Anodizing method for corrosion protection of aluminum or aluminum alloy elements used in aircraft structures
US12385155B2 (en) 2022-04-29 2025-08-12 Airbus Operations Gmbh Methods for anodizing a part surface and subsequently coating the anodized part surface for corrosion protection purposes
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