US3758390A - Novel cromium plating compositions - Google Patents

Novel cromium plating compositions Download PDF

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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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chromium
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H Chessin
M Best
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M&T HARSHAW
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M&T Chemicals Inc
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    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D3/00—Electroplating: Baths therefor
    • C25D3/02—Electroplating: Baths therefor from solutions
    • C25D3/04—Electroplating: Baths therefor from solutions of chromium
    • C25D3/10—Electroplating: Baths therefor from solutions of chromium characterised by the organic bath constituents used
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D3/00—Electroplating: Baths therefor
    • C25D3/02—Electroplating: Baths therefor from solutions
    • C25D3/04—Electroplating: 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)

Abstract

THIS INVENTION RELATES TO NOVEL COMPOSITIONS AND TO 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: (1) 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 (2) AT LEAST ONE MEMBER OF THE GROUP CONSISTING OF SULFOACETIC ACID, ISETHIONATE AND ISETHIONIC ACID; FOR A TIME SUFFICIENT TO DEPOSIT A CHROMIUM ELECTROPLATE HAVING A THICKNESS OF AT LEAST 1X10**-4 MILLIMETER.

Description

United States Patent 3,758,390 NOVEL CHROMIUM PLATING COMPOSITIONS Hyman Chessin, Birmingham, Mich., and Maurice P. Best, Streetly, England, assignors to M & T Chemicals Inc., Greenwich, Conn. No Drawing. Filed June 18, 1971, Ser. No. 154,703 Int. Cl. C23b /06 US. Cl. 204-51 14 Claims ABSTRACT OF THE DISCLOSURE This invention relates to novel compositions and to 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:
( 1) 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
(2) at least one member of the group consisting of sulfoacetic acid, isethionate and isethionic acid; for a time suflicient to deposit a chromium electroplate having a thickness of at least 1X10" millimeter.
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.
The hardness of chromium delays the proper seating, or formation of a tight joint. As a practical matter, it is not possible to machine all moving parts to tolerances which will provide an exact fit and, ordinarily, conformation of the parts is obtained during an initial period of actual operation which causes the parts to accommodate themselves to one another. This process of accommodation is generally referred to as breaking-in.
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.
Other objects of the invention will be apparent to those skilled in the art upon inspection of the following detailed description of the invention.
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:
( 1) 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
(2) at least one member of the group consisting of sulfoacetic acid, isethionate and isethionic acid.
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.
According to another of its aspects 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:
(l)helectrodepositing a hard chromium first layer and t en (2) electrodepositing on said first layer of hard chromium a layer of microcrack chromium having at least 40 cracks per centimeter comprising maintaining an aqueous chromium plating bath containing chromic acid, sulfate ions, active fluoride ions, and at least one member of the group consisting of:
(a) sulfoacetic acid (b) isethionate (c) isethionic acid According to another of its aspects 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.
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.
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 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. Typically, 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.
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. Examples of 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.
Preferably, 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. The presence of 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. Typically, 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.
In accordance with certain embodiments of this invention, 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. When 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. Typically, from about 1 gram per liter to 4 grams per liter or more of CeF (or other cerous salts including complex fluoride salts) may be added to 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 The following examples are submitted for the purpose of illustration only and are not to be construed as limiting the scope of the invention in any way.
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 A 500 milliliter Hull Cell was used with an all soluble salt bath of the following composition:
G./l. OzJgal.
Chromic acid (CrO3) 175 23. 4 Sulfate (S04) 0.875 0. 117 Fluosilieatc (Si Fa") O. 375 0. 050
EXAMPLE 3 Hull Cell panels were also plated using the following chromium plating bath composition:
G./l. Oz./gal.
Chromic acid (CrOa) 175 23. 4 Sulfate (804-) 0. 58 0. 08 Sodium sulfate (NazSOr) 0. 86 0.11 Fluoride F-) 0.30 0. 04 Cerous fluoride (Cel 2. 50 0.33
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.
Although this invention has been illustrated by reference to specific embodiments, modifications thereof which are clearly within the scope of the invention will be apparent to those skilled in the art.
We claim:
1. 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:
(1) grams per liter to 600 grams per liter of at least one chromium compound providing hexavalent chromium ions for electroplating chromium; at least one catalyst selected from the group comprising 0.2 gram per liter to 5.0 grams per liter of sulfate ions and 0.0005 mole per liter to 0.15 mole per liter of fluoride ions; and
(2) 1 gram per liter to 10 grams per liter of at least one member of the group consisting of sulfoacetic acid, isethionate and isethionic acid; for a time sufficient to deposit a chromium electroplate having a thickness of at least IX 10 millimeter.
2. The process of claim 1 wherein said process is one for electrodepositing a bright decorative chromium plate and said isethionate is sodium isethionate.
3. A process for electroplating chromium plate onto a basis metal as claimed in claim 1 wherein the aqueous acidic chromium plating solution contains about 100-600 grams per liter of chromic acid.
4. A process for electroplating chromium plate onto a basis metal as claimed in claim 1 wherein the electroplating process is carried out at 30-70 C.
5. A process for electroplating chromium plate onto a basis metal as claimed in claim 1 wherein the aqueous acidic chromium plating solution contains about 100-600 grams per liter of chromic acid and is saturated with a cerous salt at 30-70 C.
6. A process for electroplating chromium plate onto a basis metal as claimed in claim 1 wherein the aqueous acidic chromium plating solution contains about 100-600 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.
7. A process for electroplating chromium plate onto a basis metal as claimed in claim 1' wherein the 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.
8. A process for electroplating chromium plate onto a basis metal as claimed in claim 1 wherein the 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.
9. A composition for electroplating chromium plate onto a basis metal which comprises:
(1) 100 grams per liter to 600 grams per liter of at least one chromium compound providing hexavalent chromium ions in aqueous media for electroplating chromium, 0.2 grams per liter to 5.0 grams per liter of sulfate ions as catalysts; and
(2) 1 gram per liter to grams per liter of at least one member of the group consisting of sulfoacetic acid, isethionate and isethionic acid.
10. A composition for electroplating chromium plate onto a basis metal as claimed in claim 6 wherein the concentration of chromic acid is about 100-600 grams per liter.
11. A composition for electroplating chromium plate onto a basis metal as claimed in claim 6 wherein the concentration of chromic acid is about 200-350 grams per liter and the composition for electroplating is saturated with a cerous salt at 30-70" C.
12. A composition for electroplating bright decorative chromium plate onto a basis metal as claimed in claim 6 wherein the concentration of chromic acid is about 200- 350 grams per liter and the composition for electroplating contains about 3.0 grams per liter of at least one member of the group consisting of sulfoacetic acid, isethionate, and isethionic acid.
13. A composition for electroplating chromium plate onto a basis metal as claimed in claim 6 wherein the concentration of chromic acid is 200-350 grams per liter and the composition for electroplating contains l-4 grams per liter of CeF 14. A composition for electroplating chromium plate onto a basis metal as claimed in claim 6 wherein the concentration of chromic acid is about 200-400 grams per liter, the chromic acid to sulfate ion ratio is -550z1, and the composition for electroplating contains about 3 grams per liter of at least one member of the group consisting of sulfoacetic acid, isethionate and isethionic acid.
References Cited UNITED STATES PATENTS 2,750,334 6/1956 Brown 20451 2,846,380 8/1958 Brown 20451 3,634,211 1/1972 Seyb 20451 FOREIGN PATENTS 1,407,483 6/ 1965 France 2045 1 FREDERICK C. EDMUNDSON, Primary Examiner US. Cl. X.R.
204DIG. 2
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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

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FR2529511A1 (en) * 1982-07-02 1984-01-06 Nouel Jean Marie OFFSET PLATES BASED STEEL AND CHROME MULTILAYER
DE3402554A1 (en) * 1984-01-26 1985-08-08 LPW-Chemie GmbH, 4040 Neuss DEPOSITION OF HARD CHROME ON A METAL ALLOY FROM AN AQUEOUS ELECTROLYTE CONTAINING CHROME ACID AND SULFURIC ACID
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
DE102005059367B4 (en) * 2005-12-13 2014-04-03 Enthone Inc. Electrolytic composition and method of depositing crack-free, corrosion-resistant and hard chromium and chromium alloy layers
RU2762695C1 (en) * 2020-11-20 2021-12-22 Федеральное государственное бюджетное образовательное учреждение высшего образования "Московский автомобильно-дорожный государственный технический университет (МАДИ)" Method for electrolytic chromium plating

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FR1255874A (en) * 1959-05-28 1961-03-10 Metal & Thermit Corp Electrolytic chrome plating process
FR1407483A (en) * 1963-09-11 1965-07-30 Udylite Corp Improvements to electrolytic chrome baths
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
AU4356372A (en) 1974-01-03
US3804728A (en) 1974-04-16
DE2229883A1 (en) 1972-12-21
FR2142014B1 (en) 1977-12-23
GB1378973A (en) 1975-01-02
FR2142014A1 (en) 1973-01-26
NL7208359A (en) 1972-12-20
AU465824B2 (en) 1975-10-09

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