US3207679A - Method for electroplating on titanium - Google Patents

Method for electroplating on titanium Download PDF

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US3207679A
US3207679A US26432A US2643260A US3207679A US 3207679 A US3207679 A US 3207679A US 26432 A US26432 A US 26432A US 2643260 A US2643260 A US 2643260A US 3207679 A US3207679 A US 3207679A
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titanium
substrate
bath
electroplating
coating
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US26432A
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Francis J Schmidt
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American Potash and Chemical Corp
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American Potash and Chemical Corp
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    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D5/00Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
    • C25D5/34Pretreatment of metallic surfaces to be electroplated
    • C25D5/38Pretreatment of metallic surfaces to be electroplated of refractory metals or nickel
    • 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
    • C25D11/26Anodisation of refractory metals or alloys based thereon

Definitions

  • This invention relates to the anodizing of titanium and titanium alloys to provide a surface suitable for subsequent electroplating or finishing.
  • titanium on exposure to air or oxidizing conditions forms a surface skin consisting chiefly of oxides which interfere with the adhesion of electrodeposited coatings.
  • the known techniques for preparation of a titanium surface for electroplating include various procedures for removal of this oxide skin to expose a clean titanium metal surface or for replacing the oxide film with a hydride film. These procedures may provide a suitable surface for cathodic deposition of metals and alloys. However, they fail as a preparatory step for anodic deposition because of the uncontrolled reformation of the oxide skin under the anodic conditions.
  • the present invention eliminates these restrictions. It also provides a process which has particular application in the plating of lead dioxide over a precious metal flash coated on a substrate of titanium or a titanium alloy. This process requires first a cathodic and then an anodic deposition on the metal base.
  • a further object is to provide a titanium surface finish which is of uniform texture and thickness and which provides excellent anchorage for dyes, paints and chemical conversion finishes.
  • a further object of this method is to provide a suitable titanium surface for electroplating, without strong etching of the titanium, thereby permitting close control of dimensional tolerances.
  • a further object is to eliminate the need for lengthy heat treatment of plated titanium articles to relieve hydrogen embrittlement.
  • a specific object of this invention is to provide a technique for electrodepositing anodically a metal oxide coating, such as lead dioxide, over a titanium, titanium alloy, or flash-coated titanium substrate.
  • the titanium substrate is anodized under controlled conditions to a yellow color.
  • the resulting oxide film is sufficiently porous to permit direct substrate metal to noble metal bonding and direct noble metal to lead dioxide bonding.
  • adhesion of the lead dioxide to the substrate by mechanical anchorage Within the spongy anodized structure is improved while further growth of the oxide skin is obviated.
  • EXAMPLE I To illustrate the practice of the invention, sheets of titanium and titanium alloy, size 8" x 4" x A were treated.
  • the titanium sheet was relatively pure, 99+%, while the titanium alloy contained 2% molybdenum, 2% chromium and 2% iron.
  • the substrate was first degreased by soaking in a 10% NaOH solution at 75.
  • the substrate After rinsing, the substrate was freed of a major portion of its oxide film. This can be achieved in various ways, usually by treatment with a suitable non-oxidizing acid at an elevated temperature since such oxide films are 3,207,679 Patented Sept. 21, 1965 ordinarily resoluble in hot acid. In the case of the plating operation under discussion, the substrate was immersed in approximately 10% HF at room temperature for several seconds, until the surface was uniformly gray and clean.
  • the substrate After rinsing the substrate was placed in 'an electrolytic cell in which the electrolyte was a 2% nitric acid solution at ambient temperature. The voltage was slowly raised from zero to about 4 volts when formation of a pale yellow anode film became visible. This voltage was maintained for about ten minutes.
  • the pale yellow color is a good measure of the desired thickness of the surface layer of oxide on the substrate, being an interference color of the light reflected from the substrate through the oxide layer applied, which defines a definite thickness.
  • the color of the applied anodized surface is a function of the value of the voltage applied. For example, using the same bath at the same temperature and applying the voltage indicated for a short period gives a film of the indicated color using the same base. The color appears in a matter of seconds; in the case of the light yellow color, the film color is apparent in about 10 seconds.
  • Example II Color Approximate voltage Slightly discolored base 1 Light yellow 4 Brown 6 Purple 8 Catastrophic corrosion 12 EXAMPLE II The procedure of Example I was followed except that similar sheets were anodized to a yellow color in a 2% NaOH solution.
  • the substrates could have been plated cathodically in another electroplating bath or, immediately following the anodizing step, in Baths 1 or 2 without first applying an intermediate cathodic flashcoating.
  • the thickness of the flash intermediate coatings has no bearing on the adhesion of the final lead dioxide coating, provided the metal or alloy used for the intermediate coating is not attacked in the lead dioxide plating solution. In the above example precious metals were used.
  • Igepal and Tergitol refer respectively to an alkylphenolethylene oxide condensation product and to a higher sodium alkyl sulphate, both useful as wetting and emulsifying agents.
  • EXAMPLE IV A' titanium sheet was prepared as in Example I. It was then anodized in a Watts nickel bath for thirty seconds, at a constant voltage of 4. The current density was 20-100 amps. sq. ft. and the bath temperature was between 115-160 F. The bath had the following composition:

Description

United States Patent 3,207,679 METHGD FOR ELECTROPLATING UN TITANIUM Francis J. Schmidt, Las Vegas, Nev., assignor to American Potash & Chemical Corporation, a corporation of Delaware No Drawing. Filed May 3, 1960, Ser. No. 26,432
3 Claims. (Cl. 204-42) This invention relates to the anodizing of titanium and titanium alloys to provide a surface suitable for subsequent electroplating or finishing.
It is known that titanium on exposure to air or oxidizing conditions forms a surface skin consisting chiefly of oxides which interfere with the adhesion of electrodeposited coatings. The known techniques for preparation of a titanium surface for electroplating include various procedures for removal of this oxide skin to expose a clean titanium metal surface or for replacing the oxide film with a hydride film. These procedures may provide a suitable surface for cathodic deposition of metals and alloys. However, they fail as a preparatory step for anodic deposition because of the uncontrolled reformation of the oxide skin under the anodic conditions.
The present invention eliminates these restrictions. It also provides a process which has particular application in the plating of lead dioxide over a precious metal flash coated on a substrate of titanium or a titanium alloy. This process requires first a cathodic and then an anodic deposition on the metal base.
A further object is to provide a titanium surface finish which is of uniform texture and thickness and which provides excellent anchorage for dyes, paints and chemical conversion finishes.
A further object of this method is to provide a suitable titanium surface for electroplating, without strong etching of the titanium, thereby permitting close control of dimensional tolerances.
A further object is to eliminate the need for lengthy heat treatment of plated titanium articles to relieve hydrogen embrittlement.
A specific object of this invention is to provide a technique for electrodepositing anodically a metal oxide coating, such as lead dioxide, over a titanium, titanium alloy, or flash-coated titanium substrate.
In accordance with the present invention, the titanium substrate is anodized under controlled conditions to a yellow color. The resulting oxide film is sufficiently porous to permit direct substrate metal to noble metal bonding and direct noble metal to lead dioxide bonding. In addition, adhesion of the lead dioxide to the substrate by mechanical anchorage Within the spongy anodized structure is improved while further growth of the oxide skin is obviated.
While a great number of alkaline, neutral and acidic media are suitable for the production of an anodized base for later cathodic depositions, the best results are obtained when the pH and anion composition of the anodizing and plating solutions are similar.
EXAMPLE I To illustrate the practice of the invention, sheets of titanium and titanium alloy, size 8" x 4" x A were treated. The titanium sheet was relatively pure, 99+%, while the titanium alloy contained 2% molybdenum, 2% chromium and 2% iron. The substrate was first degreased by soaking in a 10% NaOH solution at 75.
After rinsing, the substrate was freed of a major portion of its oxide film. This can be achieved in various ways, usually by treatment with a suitable non-oxidizing acid at an elevated temperature since such oxide films are 3,207,679 Patented Sept. 21, 1965 ordinarily resoluble in hot acid. In the case of the plating operation under discussion, the substrate was immersed in approximately 10% HF at room temperature for several seconds, until the surface was uniformly gray and clean.
After rinsing the substrate was placed in 'an electrolytic cell in which the electrolyte Was a 2% nitric acid solution at ambient temperature. The voltage was slowly raised from zero to about 4 volts when formation of a pale yellow anode film became visible. This voltage was maintained for about ten minutes. The pale yellow color is a good measure of the desired thickness of the surface layer of oxide on the substrate, being an interference color of the light reflected from the substrate through the oxide layer applied, which defines a definite thickness. The color of the applied anodized surface is a function of the value of the voltage applied. For example, using the same bath at the same temperature and applying the voltage indicated for a short period gives a film of the indicated color using the same base. The color appears in a matter of seconds; in the case of the light yellow color, the film color is apparent in about 10 seconds.
Color Approximate voltage Slightly discolored base 1 Light yellow 4 Brown 6 Purple 8 Catastrophic corrosion 12 EXAMPLE II The procedure of Example I was followed except that similar sheets were anodized to a yellow color in a 2% NaOH solution.
EXAMPLE III Following the anodization of Examples I and II, each substrate was rinsed and then flashplated with platinum in the usual manner in a bath having the following composition:
Water liter 1 Diammonium phosphate grams 20 Disodium phosphate do Chloroplatinic acid do 4 The substrates, now flashplated with a layer of platinum, were then coated with lead dioxide in baths of the following composition:
0.1/1. of a non-ionic wetting agent, Tergitol.
The substrates could have been plated cathodically in another electroplating bath or, immediately following the anodizing step, in Baths 1 or 2 without first applying an intermediate cathodic flashcoating. The thickness of the flash intermediate coatings has no bearing on the adhesion of the final lead dioxide coating, provided the metal or alloy used for the intermediate coating is not attacked in the lead dioxide plating solution. In the above example precious metals were used.
The trademarks Igepal and Tergitol refer respectively to an alkylphenolethylene oxide condensation product and to a higher sodium alkyl sulphate, both useful as wetting and emulsifying agents.
EXAMPLE IV A' titanium sheet was prepared as in Example I. It Was then anodized in a Watts nickel bath for thirty seconds, at a constant voltage of 4. The current density was 20-100 amps. sq. ft. and the bath temperature Was between 115-160 F. The bath had the following composition:
Ounces/ gallon Nickel sulfate 32 Nickel chloride 6 Boric acid 4 Subsequently, Without removing the article from the bath, the polarity was reversed and nickel Was deposited on the article for one minute. Such nickel flashcoats function Well as a base for a great variety of electrodeposits, ineluding heavy nickel coatings. The composition of the Watts nickel bath appears at page 341 in Metal Finishing Guidebook (1957), published by Finishing Publications, Inc., New Jersey.
In the place of titanium we can employ alloys in which titanium is a substantial alloying agent.
I claim:
1. In a process for preparing an electrode having a titanium substrate, the steps comprising:
(a) anodizing the titanium substrate in a first bath to a yellow color,
(b) cathodically applying a flash coating of platinum upon the anodized titanium substrate in a bath having substantially the same anion concentration and pH as the first bath, and thereafter electroplating a coating of lead dioxide onto the flash coated platinum.
2. In a process for preparing an electrode having a titanium substrate, the steps comprising:
(a) placing the titanium substrate, as an anode, in an electrolyte containing a cathode, applying current to the substrate-anode and increasing the voltage to deposit a yellow layer of titanium oxide upon the surface of said titanium substrate,
(b) cathodically applying a flash coating of platinum upon the layer of titanium oxide deposited in (a), and thereafter (c) electroplating a coating of lead dioxide onto the flash coated platinum.
3. In a process for preparing an electrode having a titanium substrate, the steps comprising:
(a) placing the titanium substrate, as an anode, in an electrolyte containing a cathode, applying current to the substrate-anode and increasing the voltage to about four volts and maintaining that voltage for about 10 minutes to deposit a layer of titanium oxide upon the surface of said titanium substrate,
(b) cathodically applying a flash coating of platinum upon the layer of titanium oxide deposited in (a), and thereafter (c) electrolytically depositing a coating of lead dioxide upon the layer of platinum deposited in (b).
References Qited by the Examiner UNITED STATES PATENTS 2,711,496 6/55 Ruben 20442 2,851,405 9/58 Dymon et al 204-42 2,945,791 7/60 Gibson 204-57 2,949,411 8/60 Beck 204-56 2,955,999 10/60 Tirrell. 2,965,551 12/60 Richaud 204-56 2,999,799 9/61 Saubestre et al. 20442 FOREIGN PATENTS 221,757 6/59 Australia. 586,846 11/59 Canada.
WINSTON A. DOUGLAS, Primary Examiner.
JOHN R. SPECK, JOHN H. MACK, Examiners.

Claims (1)

1. IN A PROCESS FOR PREPARING AN ELECTRODE HAVING A TITANIUM SUBSTRATE, THE STEPS OF COMPRISING: (A) ANODIZING THE TITANIUM SUBSTRATE IN A FIRST BATH TO A YELLOW COLOR, (B) CATHODICALLY APPLYING A FLASH COATING OF PLATINUM UPON THE ANODIZED TITANIUM SUBSTRATE IN A BATH HAVING SUBSTANTIALLY THE SAME ANION CONCENTRATION AND PH AS THE FIRST BATH, AND THEREAFTER (C) ELECTROPLATING A COATING OF LEAD DIOXIDE ONTO THE FLASH COATED PLATINUM.
US26432A 1960-05-03 1960-05-03 Method for electroplating on titanium Expired - Lifetime US3207679A (en)

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Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4008144A (en) * 1974-08-22 1977-02-15 Agency Of Industrial Science & Technology Method for manufacturing of electrode having porous ceramic substrate coated with electrodeposited lead dioxide and the electrode manufactured by said method
US4038170A (en) * 1976-03-01 1977-07-26 Rhees Raymond C Anode containing lead dioxide deposit and process of production
US4040939A (en) * 1975-12-29 1977-08-09 Diamond Shamrock Corporation Lead dioxide electrode
US4051000A (en) * 1974-11-04 1977-09-27 The International Nickel Company, Inc. Non-contaminating anode suitable for electrowinning applications
US4278522A (en) * 1978-08-23 1981-07-14 Bbc Brown Boveri & Company Limited Apparatus for treating contaminated water
US4415411A (en) * 1980-03-04 1983-11-15 The Japan Carlit Co., Ltd. Anode coated with β-lead dioxide and method of producing same
US4510034A (en) * 1982-08-31 1985-04-09 Asahi Kasei Kogyo Kabushiki Kaisha Coating type insoluble lead dioxide anode
US4765335A (en) * 1987-03-16 1988-08-23 Intermar, Inc. Aneurysm clip
WO2007059730A2 (en) * 2005-11-21 2007-05-31 Mtu Aero Engines Gmbh Method for the pre-treatment of titanium components for the subsequent coating thereof
US20220042964A1 (en) * 2019-04-29 2022-02-10 Shenzhen Angel Drinking Water Industrial Group Corporation Water hardness detection probe, sensor, detection method and water softener

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2711496A (en) * 1952-09-27 1955-06-21 Ruben Samuel Lead peroxide rectifiers and method of making the same
US2851405A (en) * 1953-07-03 1958-09-09 Sylvania Electric Prod Titanate rectifiers
CA586846A (en) * 1959-11-10 C. Miller Henry Electrode, its preparation and use
US2945791A (en) * 1958-03-05 1960-07-19 Jr Fred D Gibson Inert lead dioxide anode and process of production
US2949411A (en) * 1957-05-13 1960-08-16 Titanium Metals Corp Titanium anodizing process
US2955999A (en) * 1957-09-04 1960-10-11 Ionics Self-rectifying electrodialysis unit
US2965551A (en) * 1956-08-08 1960-12-20 Pechiney Prod Chimiques Sa Metal plating process
US2999799A (en) * 1958-06-26 1961-09-12 Sylvania Electric Prod Electroplating of niobium

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA586846A (en) * 1959-11-10 C. Miller Henry Electrode, its preparation and use
US2711496A (en) * 1952-09-27 1955-06-21 Ruben Samuel Lead peroxide rectifiers and method of making the same
US2851405A (en) * 1953-07-03 1958-09-09 Sylvania Electric Prod Titanate rectifiers
US2965551A (en) * 1956-08-08 1960-12-20 Pechiney Prod Chimiques Sa Metal plating process
US2949411A (en) * 1957-05-13 1960-08-16 Titanium Metals Corp Titanium anodizing process
US2955999A (en) * 1957-09-04 1960-10-11 Ionics Self-rectifying electrodialysis unit
US2945791A (en) * 1958-03-05 1960-07-19 Jr Fred D Gibson Inert lead dioxide anode and process of production
US2999799A (en) * 1958-06-26 1961-09-12 Sylvania Electric Prod Electroplating of niobium

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4008144A (en) * 1974-08-22 1977-02-15 Agency Of Industrial Science & Technology Method for manufacturing of electrode having porous ceramic substrate coated with electrodeposited lead dioxide and the electrode manufactured by said method
US4051000A (en) * 1974-11-04 1977-09-27 The International Nickel Company, Inc. Non-contaminating anode suitable for electrowinning applications
US4040939A (en) * 1975-12-29 1977-08-09 Diamond Shamrock Corporation Lead dioxide electrode
US4038170A (en) * 1976-03-01 1977-07-26 Rhees Raymond C Anode containing lead dioxide deposit and process of production
US4278522A (en) * 1978-08-23 1981-07-14 Bbc Brown Boveri & Company Limited Apparatus for treating contaminated water
US4415411A (en) * 1980-03-04 1983-11-15 The Japan Carlit Co., Ltd. Anode coated with β-lead dioxide and method of producing same
US4510034A (en) * 1982-08-31 1985-04-09 Asahi Kasei Kogyo Kabushiki Kaisha Coating type insoluble lead dioxide anode
US4765335A (en) * 1987-03-16 1988-08-23 Intermar, Inc. Aneurysm clip
WO2007059730A2 (en) * 2005-11-21 2007-05-31 Mtu Aero Engines Gmbh Method for the pre-treatment of titanium components for the subsequent coating thereof
WO2007059730A3 (en) * 2005-11-21 2007-10-11 Mtu Aero Engines Gmbh Method for the pre-treatment of titanium components for the subsequent coating thereof
US20090218232A1 (en) * 2005-11-21 2009-09-03 Mtu Aero Engines Gmbh Method for the Pre-Treatment of Titanium Components for the Subsequent Coating Thereof
US8354036B2 (en) 2005-11-21 2013-01-15 Mtu Aero Engines Gmbh Method for the pre-treatment of titanium components for the subsequent coating thereof
US20220042964A1 (en) * 2019-04-29 2022-02-10 Shenzhen Angel Drinking Water Industrial Group Corporation Water hardness detection probe, sensor, detection method and water softener
US11927584B2 (en) * 2019-04-29 2024-03-12 Shenzhen Angel Drinking Water Industrial Group Corporation Water hardness detection probe, sensor, detection method and water softener

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