US3788957A - Electrodeposition of chromium - Google Patents

Electrodeposition of chromium Download PDF

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Publication number
US3788957A
US3788957A US00293860A US3788957DA US3788957A US 3788957 A US3788957 A US 3788957A US 00293860 A US00293860 A US 00293860A US 3788957D A US3788957D A US 3788957DA US 3788957 A US3788957 A US 3788957A
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US
United States
Prior art keywords
chromium
plating
electrolyte solution
water
ions
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
US00293860A
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English (en)
Inventor
I Christie
J Ward
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.)
International Lead Zinc Research Organization Inc
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International Lead Zinc Research Organization Inc
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
Priority claimed from GB4568971A external-priority patent/GB1305156A/en
Application filed by International Lead Zinc Research Organization Inc filed Critical International Lead Zinc Research Organization Inc
Application granted granted Critical
Publication of US3788957A publication Critical patent/US3788957A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D3/00Electroplating: Baths therefor
    • C25D3/02Electroplating: Baths therefor from solutions
    • C25D3/04Electroplating: Baths therefor from solutions of chromium
    • C25D3/06Electroplating: Baths therefor from solutions of chromium from solutions of trivalent chromium
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D3/00Electroplating: Baths therefor
    • C25D3/02Electroplating: Baths therefor from solutions
    • C25D3/04Electroplating: Baths therefor from solutions of chromium
    • C25D3/10Electroplating: Baths therefor from solutions of chromium characterised by the organic bath constituents used

Definitions

  • This application is directed to the electrodeposition of chromium and more particularly to the use of a surfactant as an ingredient in an improved electrolyte solution.
  • chromium deposits As an improvement over chromium plating from conventional aqueous chromic acid baths, a method has been developed whereby chromium deposits, having greatly improved corrosion resistance and exhibiting a very good appearance, can be provided by electrolytic techniques through the use of a plating bath comprising chromium ions, particularly trivalent chromium ions, and a homogeneous mixture of water and a dipolar organic solvent,
  • aprotic such as dimethylformamide
  • the ratio by volume of water to dimethylformamide may range from 10:90 to 95:5 but preferably between 60:40 and :10. These lower concentrations of dimethylformamide make possible a reduction in the cost of the plating bath without necessarily impairing the plating performance.
  • the physical characteristics of the solution e.g., color, pH, and viscosity, have been found to change during storage and the color and adhesion of successive metal deposits from the same bath may deteriorate.
  • plating baths containing low concentrations of Water have a relatively low conductivity, while solutions with higher concentrations of water tend to evolve excessive amounts of hydrogen at the cathode during plating. It has been found that the presence of an ammonium salt improves the stability of the solution and reduces the tendency of the bath to evolve hydrogen at high water content.
  • ammonium salts Moreover the presence of ammonium salts has been found to significantly reduce the effect of changes in pH on the lower limiting plating current density.
  • the ammonium ion should be present at a concentration of at least about 0.2 M and preferably from about 0.6 to about 1 M. At lower concentrations of dimethylformamide, it may be preferable to increase the ammonium ion concentration to above 1 M.
  • a prerequisite of successful chromium plating from a dipolar organic solvent is that the trivalent chromium ions shall form small moderately stable complexes with the solvent molecule. If there is no complex formation, then the chromic salts are unlikely to be sufficiently soluble. If the complexes formed are excessively stable, then electrodeposition may be diflicult. It is believed that the highly electronegative oxygen atoms which characterize the dipolar organic compounds of this invention may act as covalent links in the formation of complexes between the chromic ions and the organic molecules. Such solutions by themselves do not, however, give smooth coherent metallic deposits.
  • the pH of the solution should be from 1 to 3.5 and preferably about 2. If the pH is too low, hydrogen tends to be evolved at the cathode in preference to chromium. If the pH is too high, basic chromium compounds are liable to precipitate out.
  • the pH can be adjusted by the use ofhydrochloric acid or sodium hydroxide as required.
  • the current efficiency of the solution may be improved by the addition of boric acid, preferably to a concentration of at least 0.1 M.
  • Boric acid is not normally soluble to the extent of more than about 0.2 M.
  • electroplating baths of the present invention contain a sodium halide which has been found to increase the plating range and current efliciency.
  • Sodium halides are also beneficial in that they enhance the covering power of the bath. It is preferred that the sodium halide be present in a concentration of at least about 0.8 M. Again, however, if lower concentrations of dimethylformamide are to be used, it may be advantageous to increase the halide ion concentration above 5 M, for example from 7 to 10 M.
  • the surfactant may be cationic, anionic, amphoteric or non-ionic, but cationic surfactants are preferred.
  • Nonionic surfactants tend to give rise to dull deposits, particularly when used in higher concentrations.
  • Anionic surfactants such as Na lauryl sulphate, again particularly at higher concentrations, tend to give rise to black specks on the metal deposits.
  • Cationic surfactants that may be used according to the invention are tetraalkylammonium salt of the general formula /f ⁇ R: R4 X and substituted imidazoline of the general formula wherein R is an alkyl having 8 to 18 carbon atoms, R,, R and R are alkyls having from 1 to 2 carbon atoms,
  • R is selected from the group consisting of aliphatic short chain alcohol having up to 6 carbon atoms of the general formula C H OH and sodium salt of a carboxylic acid of the general formula C H OC 'H ,CO'ONa, R is an alkyl having 9 to 17 carbon atoms, R, is an alkyle ne having 1 to 4 carbon atoms, and X is a halogen selected from the group consisting of bromine, chlorine and iodine, and n and n are 1 to 6, the proportion of water to dipolar aprotic solvent being from about :90 to about 90:10.
  • An electrolyte solution according to claim 1 having ammonium ions in a concentration of at least 0.2 M and halogen ions in a concentration at least 0.8 M.
  • An electrolyte solution according to claim 4 having halogen ions in a concentration of at least 5 M.
  • An electrolyte solution according to claim 3 having between about 5 p.p.m. and about 20 p.p.m. of said surfactant.
  • An electrolyte solution according to claim 3 having said surfactant in a concentration of between 5 p.p.m. and such amount as causes foaming of the electrolyte solution.
  • An electrolyte solution according to claim 3 having ammonium ions in a concentration of between about 0.6 M and about 1 M.
  • An electrolyte solution according to claim 3 having a pH between about 1 and 3.5.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Electroplating And Plating Baths Therefor (AREA)
US00293860A 1971-09-30 1972-10-02 Electrodeposition of chromium Expired - Lifetime US3788957A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB4566971A GB1368749A (en) 1971-09-30 1971-09-30 Electrodeposition of chromium
GB4568971A GB1305156A (enrdf_load_stackoverflow) 1970-12-10 1971-09-30

Publications (1)

Publication Number Publication Date
US3788957A true US3788957A (en) 1974-01-29

Family

ID=26265633

Family Applications (1)

Application Number Title Priority Date Filing Date
US00293860A Expired - Lifetime US3788957A (en) 1971-09-30 1972-10-02 Electrodeposition of chromium

Country Status (6)

Country Link
US (1) US3788957A (enrdf_load_stackoverflow)
AU (1) AU471915B2 (enrdf_load_stackoverflow)
DE (1) DE2247840C3 (enrdf_load_stackoverflow)
FR (1) FR2154725B1 (enrdf_load_stackoverflow)
GB (1) GB1368749A (enrdf_load_stackoverflow)
NL (1) NL7213209A (enrdf_load_stackoverflow)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3954574A (en) * 1973-12-13 1976-05-04 Albright & Wilson Limited Trivalent chromium electroplating baths and electroplating therefrom
US4053374A (en) * 1975-08-27 1977-10-11 Albright & Wilson Limited Chromium electroplating baths
USRE29749E (en) * 1973-12-13 1978-08-29 Albright & Wilson Ltd. Trivalent chromium electroplating baths and electroplating therefrom
US4472249A (en) * 1981-08-24 1984-09-18 M&T Chemicals Inc. Bright chromium plating baths and process
US20070227895A1 (en) * 2006-03-31 2007-10-04 Bishop Craig V Crystalline chromium deposit
US8187448B2 (en) 2007-10-02 2012-05-29 Atotech Deutschland Gmbh Crystalline chromium alloy deposit

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4686017A (en) * 1981-11-05 1987-08-11 Union Oil Co. Of California Electrolytic bath and methods of use
US4755265A (en) * 1985-06-28 1988-07-05 Union Oil Company Of California Processes for the deposition or removal of metals
US4801511A (en) * 1985-06-28 1989-01-31 Union Oil Company Of California Battery cell electrolyte

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1304844A (enrdf_load_stackoverflow) * 1969-04-24 1973-01-31
AU2348470A (en) * 1969-12-29 1972-07-06 International Lead Zinc Research Organization Aqueous chromium plating baths

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3954574A (en) * 1973-12-13 1976-05-04 Albright & Wilson Limited Trivalent chromium electroplating baths and electroplating therefrom
USRE29749E (en) * 1973-12-13 1978-08-29 Albright & Wilson Ltd. Trivalent chromium electroplating baths and electroplating therefrom
US4053374A (en) * 1975-08-27 1977-10-11 Albright & Wilson Limited Chromium electroplating baths
US4472249A (en) * 1981-08-24 1984-09-18 M&T Chemicals Inc. Bright chromium plating baths and process
US20070227895A1 (en) * 2006-03-31 2007-10-04 Bishop Craig V Crystalline chromium deposit
US7887930B2 (en) 2006-03-31 2011-02-15 Atotech Deutschland Gmbh Crystalline chromium deposit
US20110132765A1 (en) * 2006-03-31 2011-06-09 Bishop Craig V Crystalline chromium deposit
US8187448B2 (en) 2007-10-02 2012-05-29 Atotech Deutschland Gmbh Crystalline chromium alloy deposit

Also Published As

Publication number Publication date
NL7213209A (enrdf_load_stackoverflow) 1973-04-03
AU4721772A (en) 1974-04-04
DE2247840A1 (de) 1973-04-05
GB1368749A (en) 1974-10-02
AU471915B2 (en) 1976-05-06
FR2154725A1 (enrdf_load_stackoverflow) 1973-05-11
DE2247840C3 (de) 1978-06-08
DE2247840B2 (de) 1977-10-20
FR2154725B1 (enrdf_load_stackoverflow) 1976-06-04

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