US3758390A - Novel cromium plating compositions - Google Patents

Novel cromium plating compositions Download PDF

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Publication number
US3758390A
US3758390A US00154703A US3758390DA US3758390A US 3758390 A US3758390 A US 3758390A US 00154703 A US00154703 A US 00154703A US 3758390D A US3758390D A US 3758390DA US 3758390 A US3758390 A US 3758390A
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United States
Prior art keywords
chromium
per liter
acid
grams per
electroplating
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Expired - Lifetime
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US00154703A
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English (en)
Inventor
H Chessin
M Best
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M&T HARSHAW
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M&T Chemicals Inc
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Assigned to ATOCHEM NORTH AMERICA, INC. reassignment ATOCHEM NORTH AMERICA, INC. MERGER (SEE DOCUMENT FOR DETAILS). Assignors: ATOCHEM INC., A CORP. OF DE., M&T CHEMICALS INC., A CORP. OF DE., (MERGED INTO), PENNWALT CORPORATION, A CORP. OF PA., (CHANGED TO)
Anticipated expiration legal-status Critical
Assigned to M&T HARSHAW reassignment M&T HARSHAW ASSIGNMENT OF ASSIGNORS INTEREST. Assignors: ATOCHEM NORTH AMERICA, INC., A CORP. OF PENNSYLVANIA
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    • 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
    • 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

Definitions

  • At least one chromium compound providing hexavalent chromium ions for electroplating chromium; at least one catalyst selected from the group comprising sulfate ions and fluoride ions, and
  • This invention relates to a novel process for the electrodeposition of chromium and to the novel chromium deposits formed thereby.
  • This invention also relates to chromium surface layers on wearing parts and touching parts in relative motion, such as piston rings in cylinders, bearings, and turbine edges.
  • An object of the present invention is to provide a chromium bearing surface which has quick break-in characteristics while retaining the excellent wearing qualities and long life of such surfaces.
  • Another object of this invention is to provide a process for electrodepositing bright decorative chromium plate.
  • This invention relates to novel compositions and to a process for electroplating decorative chromium plate onto a basis metal which comprises passing current from an anode to a cathode at least a portion of which contains a conductive metal layer through an aqueous acidic chromium plating solution containing:
  • At least one chromium compound providing hexavalent chromium ions for electroplating chromium; at least one catalyst selected from the group comprising fluoride ions and sulfate ions, and
  • the chromium electroplating bath compositions of the invention contain about 100-600 grams per liter of chromic acid (expressed as CrO and preferably about 100200 grams per liter of chromic acid.
  • the plate produced by the novel process of this invention is highly satisfactory with respect to its unusually bright decorative appearance.
  • this invention is a 3,758,390 Patented Sept. 11, 1973 methodof forming a bearing surface upon a substrate comprising a duplex plating of two disparate kinds of chromium comprising:
  • this invention relates to a piston ring comprising an inner annular portion, an intermediate contiguous hard chromium portion, and an outer annular portion of microcracked chromium.
  • isethionates such as sodium isethionate
  • sulfoacetic acid While sulfoacetic acid itself imparts homogeneous microcracking, isethionates, such as sodium isethionate, are readily oxidized to sulfoacetic acid by the chromic acid plating bath and also effect enhanced microcracking of chromium. Thus it has been found that sulfoacetic acid has been found to produce a very different structure in heavy chromium deposits.
  • the amount of sulfoacetic acid added to the chromic acid bath should be between 1 gram per liter and 10 grams per liter, preferably about 3 grams per liter.
  • Sulfate ions may be added to the chromium electroplating bath in the form of suitable sulfate compounds such as strontium sulfate (SrSO sulfuric acid (H 50 lithium sulfate (Li SO ammonium sulfate calcium sulfate (CaS0 etc.
  • strontium sulfate SrSO sulfuric acid (H 50 lithium sulfate (Li SO ammonium sulfate calcium sulfate (CaS0 etc.
  • the chromium electroplating process uses temperatures of 30-70 C. with a chromic acid bath containing 600 grams per liter of chromic acid (as CrO).
  • CrO chromic acid bath containing 600 grams per liter of chromic acid
  • the ratio of chromic acid to sulfate ion (CrO :SO should be maintained at 50-550z1, typically ISO-300:1 and preferably about 200: 1.
  • the aqueous chromium plating bath contains active fluoride.
  • Active fluoride is fluoride ion in the form exhibiting catalytic activity in the bath.
  • Active fluoride may be in the form of simple fluoride, F-, or complex fluoride. Where complex fluorides are employed, one mole of complex fluoride may be considered equivalent to one mole of simple fluoride ion, i.e. both contribute approximately one mole of active fluoride to the bath.
  • the active fluoride may be selected from the group consisting of fluoride (F'), and complex fluorides including fluosilicate or silicofluoride (SiF fluoborate (BF4"), fluoaluminate (AIF fluophosphate (PFg'), fluozirconate (ZrF and fluotitanate (TiF Fluosilicate may be the most preferred active fluoride.
  • fluoride F'
  • complex fluorides including fluosilicate or silicofluoride (SiF fluoborate (BF4"), fluoaluminate (AIF fluophosphate (PFg'), fluozirconate (ZrF and fluotitanate (TiF Fluosilicate may be the most preferred active fluoride.
  • the active fluoride may typically be present in the aqueous chromium plating bath in the amount of about 0.0005- 0.l5 mole per liter. Preferably 0.01-0.05 mole per liter of active fluoride may be present.
  • the active fluoride may be introduced into the bath by dissolving therein a salt or an acid of the active fluoride. Preferably, an alkali metal salt may be employed.
  • suitable sources of active fluoride include sodium fluoride, potassium silicofluoride, fluoboric acid, sodium fluoaluminate, potassium fluophosphate, sodium bifluoride, potassium bifluoride, sodium fluotitanate, sodium fluozirconate, ammonium fluoslicate, and lithium fluosilicate.
  • the aqueous chromium plating bath also contains sulfate ion, typically in the amount of about 0.2-5.0 grams per liter and preferably 0.3-4.0 gram per liter, say 13 grams per liter.
  • sulfate ion improves the microcrack effect and the appearance of the chromium deposit and lowers plating time.
  • the sulfate ion may be provided by dissolving in the bath sulfuric acid or a salt thereof having sufiicient solubility to produce the desired concentration.
  • Suitable sources of sulfate ion include sulfuric acid, sodium sulfate, potassium sulfate, magnesium sulfate, strontium sulfate, calcium sulfate, etc.
  • the bath may contain common ion salts, e.g. K Sr+ Ca++, La+++, and other rare earth cations or mixtures thereof to limit the solubility of the catalyst ions to a desirable value in a self-regulating system.
  • the highly preferred aqueous chromium plating baths contain, in addition to chromic acid, sulfate, at least one member of the group consisting of sulfoacetic acid, isethionate and isethionic acid, active fluoride; selenium in soluble form. Soluble selenium may be introduced into the bath by dissolving therein a compound containing selenium which is soluble in the bath.
  • Illustrative useful compounds include selenic acid and salts thereof, such as sodium selenate, ammonium selenate, potassium selenate, selenous acid and salts thereof, such as sodium selenite, potassium selenite; lower alkyl esters of selenic acid and selenous acid such as dimethyl selenate, diethyl selenate, di-n-propyl selenate, di-sec-butyl selenate, dimethyl selenite, diethyl selenite, di-isopropyl selenite, di-n-butyl selenite, etc.
  • Other compounds capable of contributing selenium in soluble form may also be employed.
  • the most preferred form of solubleselenium is selenate.
  • the selenium is present in the bath in the amount of 50 10* mole per liter Se and preferably 3 l0- mole per liter Se.
  • the baths containing selenium, preferably selenate, within the noted ranges produce an exceptionally dense, fine microcrack pattern on cathodes plated according to the process of this invention.
  • the most highly preferred aqueous chromium plating baths may contain chromic acid, active fluoride preferably fluosilicate, sulfate, and selenium, preferably selenate.
  • the aqueous chromium plating bath may contain:
  • Cerous ions may be added to the bath in the form of salts such as cerium carbonate, cerium fluoride, cerium sulfate, etc.
  • cerium fluoride CeF is employed in combination with fluoride, fluoride-containing and/ or sulfate catalysts
  • the chromium plating bath composition (containing 100-600 grams per liter of CrO may be saturated with CeF Such saturation is provided to obtain self-regulation of the catalyst content of the bath.
  • CeF cerous salts including complex fluoride salts
  • a chromium plating solu-- tion containing 100-600 grams per liter Cr0 to form a chromic acid solution which contains an excess of undissolved cerium fluoride (CeF).
  • EXAMPLE 1 -A 550 milliliter Hull Cell was used with an ordinary bath containing 200 grams per liter of chromic acid and 2.0 grams per liter of sulfate and 3.0 grams per liter of sulfoacetic acid to plate brass Hull Cell panels which had been nickel plated at 10 amperes for 10 minutes. After nickel plating the panels were given a water rinse, acid dip (10% sulfuric acid) and another water rinse. The panels were then placed in a slotted Hull Cell in a polyvinyl chloride tank and plated at 8 amperes for 8 minutes. The effect of adding 3 grams per liter of sulfoacetic acid to this ordinary bath was that of enhanced microcracking.
  • Example 2 With the addition of 6 grams per liter of sulfoacetic acid using the same procedure as in Example 1, except that the plating time was 6 minutes, again enhanced microcracking was attained, substantiating that the microcracked chromium of this invention was useful for break-in and other lubricity-demanding applications.
  • a process for electroplating chromium plate onto a basis metal which comprises passing current from an anode to a cathode at least a portion of which contains a conductive metal layer through an aqueous acidic chromium plating solution containing:
  • aqueous acidic chromium plating solution contains about 200-350 grams per liter of chromic acid and about 3 grams per liter of at least one member of the group consisting of sulfoacetic acid, isethionate and isethionic acid.
  • aqueous acidic chromium plating solution contains about 200-400 grams per liter of chromic acid, about 1-4 grams per liter of cerous salt, and wherein the chromic acid to sulfate ion ratio is 100-550: 1.
  • composition for electroplating chromium plate onto a basis metal which comprises:

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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)
  • Electroplating And Plating Baths Therefor (AREA)
  • Electroplating Methods And Accessories (AREA)
US00154703A 1971-06-18 1971-06-18 Novel cromium plating compositions Expired - Lifetime US3758390A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US15470371A 1971-06-18 1971-06-18
US00262151A US3804728A (en) 1971-06-18 1972-06-12 Novel chromium plating compositions

Publications (1)

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US3758390A true US3758390A (en) 1973-09-11

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US00262151A Expired - Lifetime US3804728A (en) 1971-06-18 1972-06-12 Novel chromium plating compositions

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US (2) US3758390A (enrdf_load_stackoverflow)
AU (1) AU465824B2 (enrdf_load_stackoverflow)
DE (1) DE2229883A1 (enrdf_load_stackoverflow)
FR (1) FR2142014B1 (enrdf_load_stackoverflow)
GB (1) GB1378973A (enrdf_load_stackoverflow)
NL (1) NL7208359A (enrdf_load_stackoverflow)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3943040A (en) * 1974-09-20 1976-03-09 The Harshaw Chemical Company Microcracked chromium from a bath using an organic sulfur compound
US4810336A (en) * 1988-06-21 1989-03-07 M&T Chemicals Inc. Electroplating bath and process for depositing functional, at high efficiencies, chromium which is bright and smooth
US4828656A (en) * 1987-02-09 1989-05-09 M&T Chemicals Inc. High performance electrodeposited chromium layers
US4927506A (en) * 1989-09-14 1990-05-22 Atochem North America, Inc. High-performance electrodeposited chromium layers formed at high current efficiencies

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2529511A1 (fr) * 1982-07-02 1984-01-06 Nouel Jean Marie Plaques offset a base acier et a multicouches de chrome
DE3402554A1 (de) * 1984-01-26 1985-08-08 LPW-Chemie GmbH, 4040 Neuss Abscheidung von hartchrom auf einer metallegierung aus einem waessrigen, chromsaeure und schwefelsaeure enthaltenden elektrolyten
US4588481A (en) * 1985-03-26 1986-05-13 M&T Chemicals Inc. Chromium plating bath for producing non-iridescent, adherent, bright chromium deposits at high efficiencies and substantially free of cathodic low current density etching
RU2125125C1 (ru) * 1997-12-24 1999-01-20 Малинин Владимир Федорович Способ электролитического хромирования
RU2125126C1 (ru) * 1998-01-27 1999-01-20 Малинин Владимир Федорович Способ электролитического хромирования в низкоконцентрированном электролите
DE102005059367B4 (de) * 2005-12-13 2014-04-03 Enthone Inc. Elektrolytzusammensetzung und Verfahren zur Abscheidung rissfreier, korrosionsbeständiger und harter Chrom- und Chromlegierungsschichten
RU2762695C1 (ru) * 2020-11-20 2021-12-22 Федеральное государственное бюджетное образовательное учреждение высшего образования "Московский автомобильно-дорожный государственный технический университет (МАДИ)" Способ электролитического хромирования

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1255874A (fr) * 1959-05-28 1961-03-10 Metal & Thermit Corp Procédé de chromage électrolytique
FR1407483A (fr) * 1963-09-11 1965-07-30 Udylite Corp Perfectionnements aux bains de chromage électrolytique
US3745097A (en) * 1969-05-26 1973-07-10 M & T Chemicals Inc Electrodeposition of an iridescent chromium coating
US3634211A (en) * 1969-10-06 1972-01-11 M & T Chemicals Inc Process for electroplating chromium and electrolytes therefor

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3943040A (en) * 1974-09-20 1976-03-09 The Harshaw Chemical Company Microcracked chromium from a bath using an organic sulfur compound
US4828656A (en) * 1987-02-09 1989-05-09 M&T Chemicals Inc. High performance electrodeposited chromium layers
US4810336A (en) * 1988-06-21 1989-03-07 M&T Chemicals Inc. Electroplating bath and process for depositing functional, at high efficiencies, chromium which is bright and smooth
AU626133B2 (en) * 1988-06-21 1992-07-23 M And T Chemicals Inc. Electroplating process dor depositing bright and smooth functional chromium at high efficiencies
US4927506A (en) * 1989-09-14 1990-05-22 Atochem North America, Inc. High-performance electrodeposited chromium layers formed at high current efficiencies

Also Published As

Publication number Publication date
NL7208359A (enrdf_load_stackoverflow) 1972-12-20
AU465824B2 (en) 1975-10-09
GB1378973A (en) 1975-01-02
AU4356372A (en) 1974-01-03
FR2142014B1 (enrdf_load_stackoverflow) 1977-12-23
DE2229883A1 (de) 1972-12-21
US3804728A (en) 1974-04-16
FR2142014A1 (enrdf_load_stackoverflow) 1973-01-26

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Owner name: ATOCHEM NORTH AMERICA, INC., PENNSYLVANIA

Free format text: MERGER;ASSIGNORS:ATOCHEM INC., A CORP. OF DE.;M&T CHEMICALS INC., A CORP. OF DE., (MERGED INTO);PENNWALT CORPORATION, A CORP. OF PA., (CHANGED TO);REEL/FRAME:005305/0866

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Effective date: 19910424