WO2017184380A1 - Dark colored chromium based electrodeposits - Google Patents

Dark colored chromium based electrodeposits Download PDF

Info

Publication number
WO2017184380A1
WO2017184380A1 PCT/US2017/026951 US2017026951W WO2017184380A1 WO 2017184380 A1 WO2017184380 A1 WO 2017184380A1 US 2017026951 W US2017026951 W US 2017026951W WO 2017184380 A1 WO2017184380 A1 WO 2017184380A1
Authority
WO
WIPO (PCT)
Prior art keywords
trivalent chromium
electrolyte
amino acids
chromium
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.)
Ceased
Application number
PCT/US2017/026951
Other languages
French (fr)
Inventor
Masahiro Hara
Tatsuya Nishiyama
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.)
MacDermid Acumen Inc
Original Assignee
MacDermid Acumen 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
Application filed by MacDermid Acumen Inc filed Critical MacDermid Acumen Inc
Priority to EP17786348.7A priority Critical patent/EP3443145A4/en
Priority to KR1020187033624A priority patent/KR20180137531A/en
Priority to CA3020402A priority patent/CA3020402A1/en
Priority to CN201780024363.0A priority patent/CN109154092A/en
Priority to MX2018012675A priority patent/MX2018012675A/en
Priority to BR112018071355A priority patent/BR112018071355A2/en
Priority to JP2018555269A priority patent/JP2019516016A/en
Publication of WO2017184380A1 publication Critical patent/WO2017184380A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

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
    • C25D3/10Electroplating: 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
    • C25D3/06Electroplating: Baths therefor from solutions of chromium from solutions of trivalent chromium

Definitions

  • the present invention generally relates to a composition and method for producing dark coloured chromium coatings by electrodeposition.
  • Chromium has been used for many years as a decorative coating and has many applications.
  • the chromium is generally applied as a thin coating, which is typically less than 1 micrometre in thickness, over a coating of nickel.
  • the chromium provides a hard, wear resistant layer and excellent corrosion performance is also obtained due to the chromium layer being cathodic with respect to the underlying nickel deposit.
  • the underlying nickel becomes the anode in the corrosion cell and corrodes preferentially leaving the chromium layer uncorroded.
  • these thin decorative chromium layers have been applied by electrodeposition from electrolytes based on hexavalent chromium, which typically comprise chromic acid.
  • the chromium deposits obtained from these electrolytes are essentially pure chromium and have a uniform and invariant colour.
  • a thin oxide layer forms on the top of the coatings giving a blue/white appearance which is very well known.
  • An initial solution to providing a darker hued deposit from chromium electrolytes can be obtained by electrodepo siting the chromium coatings from electrolytes based on trivIER chromium. Due to the nature of the deposition mechanism from these electrolytes, the chromium coating produced is less pure than that produced from hexavalent electrolytes. This is due to co-deposition of other elements within the coating. Most commonly, these co- deposited elements are iron, sulphur and carbon or combinations thereof. By adjusting the electrolyte formulation of trivending chromium based processes to maximize the darkness of the deposit produced by the incorporation of these co-deposited elements, coatings of a fairly dark hue can be obtained.
  • composition for a trivalent chromium electrolyte comprising:
  • amino acids comprise a cationic side chain comprising nitrogen and wherein the cationic side chain is at least essentially free of sulfur;
  • electrolyte is substantially free of hexavalent chromium salts.
  • a method for producing a dark colored chromium deposit on a substrate comprising the steps of: i. providing a trivalent chromium based electrolyte comprising:
  • amino acids comprise a cationic side chain comprising nitrogen and wherein the cationic side chain is at least essentially free of sulfur;
  • electrolyte is substantially free of hexavalent chromium salts
  • Figure 1 depicts various classes of amino acids. DETAILED DESCRIPTION OF THE PREFERED EMBODIMENTS
  • the inventors have surprisingly found that the incorporation of select amino acids which comprise nitrogen containing side chains into the trivalent chromium electrolyte results in coatings which are substantially darker than those obtained from the same electrolyte in the absence of these compounds.
  • the amino acids useful in the current invention are additionally at least essentially free of sulfur. By essentially free of sulfur, it is meant that sulfur is not present in any concentration, aside from trace amounts that may occur as contaminants in such compounds.
  • the darkest coatings are obtained when select amino acids are added to electrolytes which have already been optimised to produce dark coatings by the incorporation of other elements such as sulfur, iron, carbon or combinations thereof.
  • Amino acids fall into several groups as shown in Figure 1.
  • the amino acids methionine and cysteine (and cystine) contain bivalent sulphur in their side chains.
  • the use of these sulphur-containing compounds as darkening agents in trivalent chromium baths has been previously disclosed, as for example in WO 2012/150198A1 to Schulz et al., which is hereby incorporated herein by reference in its entirety. This is understood to be a function of the presence of sulfur in the compound, as sulfur is known to cause darker hues in trivalent chromium deposits as compared to the more pure deposits produced from hexavalent chromium electrolytes.
  • the inventors of the present invention have surprisingly found that sulfur-free amino acids, including those selected from the group having nitrogen containing cationic side chains, have the desired effect of darkening the deposit in a uniform manner.
  • the side chains are cationic under the normal pH conditions of most commercially available trivalent chromium electroplating baths (pH 2.5 - 4.0) due to the presence of a nitrogen-containing (amine) functional group in the side chain.
  • the amino acids that are useful in the current invention include, for example, arginine, histidine, lysine and combinations thereof. It was found that these amino acids will produce significant darkening of the trivalent chromium deposits. Additionally tryptophan, although not listed under the amino acids containing a positively charged group in Figure 1 , has a nitrogen-containing side chain and is also found to have enhanced darkening effects. From this result, while not wishing to be bound by theory, it is also believed that the side chain of tryptophan is cationic under the normal pH conditions in the trivalent chromium electroplating bath.
  • the effective concentration range of the preferred amino acids in the trivalent chromium electrolyte is preferably between about 1 g L and about 50 g/1 and more preferably between about 2 g/L and about 20 g 1.
  • the concentration of amino acids in the trivalent chromium electrolyte is most preferably between about 5 g/L and about 10 g/L.
  • inert anodes such as carbon anodes
  • inert anodes such as carbon anodes
  • Other inert anodes such as platinized titanium, platinum, iridium oxide coated titanium, or tantalum oxide coated titanium may also be used.
  • the temperature of the trivalent chromium based electrolyte is in the range of 40°C to 60°C, most preferably around 50°C.
  • the pH of the electrolyte is in the range from about 2 to about 5, most preferably about 3.5.
  • the current used during plating is in the range of about 1 amp to about 10 amps, most preferably about 4 amps. Agitation is not required during the plating of substrates in the trivalent chromium electrolyte.
  • the term "about” refers to a measurable value such as a parameter, or a concentration or the like and is meant to include variations of +/- 15% or less, preferably variations of +/- 10% or less, more preferably variations of +/- 5% or less, and most preferably variations of +/- 0.1 % or less from the particularly recited value in so far as such variations are appropriate to carry out the invention as described herein. Furthermore, it is also to be understood that the value to which the modifier "about” refers is itself specifically disclosed herein.
  • the substrate comprises nickel deposited on the underlying substrate and the chromium is electroplated on the nickel deposit.
  • a Konica Minolta CM2600d spectrophotometer was used to determine the "lightness" values of the various deposits by measuring the L* value according to the L*a*b* colorspace system.
  • the colorspace system gives a quantitative value (L*), which can be used to compare the degree of darkening obtained by the various combinations of amino acid additives. The higher the L* value, the lighter the deposit and the lower the L* value the darker the deposit.
  • An L* value of 0 is black and an L* of 100 is white. Lower L* values are the desire of the current invention.
  • Dark hued coatings produced by the electrodeposition of trivalent chromium using the electrolytes described herein preferably have an L* value, measured according to an L*a*b* colorspace system, of less than that of typical trivalent chromium deposits that produce light colored coatings and those that have already been maximized for darkness in the resulting deposits.
  • the trivalent chromium based electrolytes may contain thiocyanate ions.
  • the thiocyanate ions may be present in a concentration anywhere from about 0.2 g/L up to about 5.0 g/L.
  • the trivalent chromium based electrolytes presented herein are at least substantially free of hexavalent chromium salts, wherein no Cr(VI) ions can be detected in the electrolyte by ordinary measurement techniques.
  • the trivalent chromium electrolyte comprises a source of trivalent chromium ions, one or more complexants (complexing agents) capable of maintaining the trivalent chromium ions in solution, and the select amino acids as described herein.
  • the amino acids have provided darker hues in the plated deposit compared to the use of the same electrolyte without such amino acids.
  • the trivalent chromium electrolyte used as a standard is an electrolyte designed to produce light colored chromium deposits.
  • the electrolyte and plating process is based on U.S. Patent No. 4,473,448 to Deeman. This patent is hereby incorporated by reference in its entirety.
  • inventive examples are also provided based on a trivalent chromium electrolyte solution that has already been formulated to produce dark deposits, based on U.S. Patent No. 4, 161 ,432 to Barclay et al.
  • the amino acid used in the electrolyte composition is aspartic acid. This reference is hereby incorporated by reference in its entirety.
  • the lightness or L* value of the trivalent chromium deposit was measured at a point on the Hull Cell panel corresponding to a current density of 8 amps per square decimeter in all cases, which is representative of a normal working range for chromium plating.
  • Table 2 provides the L* values measured using the electrolyte based on U.S. Patent No. 4,473,448 to Deeman as a Standard (1 ), with various amino acids added that were not effective darkening agents. Table 2. Standard (1) plus 5g l Alanine 81.9
  • Example 1 Table 3 provides the L* values obtained when the amino acids described herein are added to the electrolyte based on U.S. Patent No. 4,473,448 to Deeman. The same Standard (1 ) electrolyte is used as in the comparative example above. As previously noted, this electrolyte typically produces light colored trivalent chromium deposits. Table 3.
  • the average reduction in L* value was 12.7% using the examples of the invention of arginine and histidine. This is a significant difference which can easily be seen by eye.
  • the addition of arginine, histidine or lysine gave uniform color across the entire deposit.
  • the addition of tryptophan gave a dramatic effect but produced very uneven and streaky deposits, which although significantly darker, were commercially unacceptable.
  • Table 4 gives the L* values obtained when amino acids of the invention are added to the electrolyte based on U.S. Patent No. 4, 161 ,432 to Barclay et al. This electrolyte was used as the Standard (2) to compare the L* values after the amino acids are added. As previously noted, deposits produced using this electrolyte process were previously formulated to provide dark colored trivalent chromium deposits.

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)
  • Electroplating Methods And Accessories (AREA)

Abstract

An aqueous trivalent chromium electrolyte comprising trivalent chromium ions and amino acids that allow for producing a dark colored hue in the trivalent chromium coating which is plated on a substrate. The amino acids described herein comprise a cationic side chain and are at least essentially free of sulfur. The cationic side chain of the amino acid further comprises nitrogen. When used in the trivalent chromium electrolyte, these amino acids allow for producing significantly darker trivalent chromium deposits. The trivalent chromium electrolyte is used in a method for producing the desired dark colored hue in the trivalent chromium coating that is produced on a substrate using electrodeposition.

Description

DARK COLORED CHROMIUM BASED ELECTRODEPOSITS
FIELD OF THE INVENTION
The present invention generally relates to a composition and method for producing dark coloured chromium coatings by electrodeposition.
BACKGROUND OF THE INVENTION
Chromium has been used for many years as a decorative coating and has many applications. For decorative purposes, the chromium is generally applied as a thin coating, which is typically less than 1 micrometre in thickness, over a coating of nickel. The chromium provides a hard, wear resistant layer and excellent corrosion performance is also obtained due to the chromium layer being cathodic with respect to the underlying nickel deposit. Thus the underlying nickel becomes the anode in the corrosion cell and corrodes preferentially leaving the chromium layer uncorroded.
Typically, these thin decorative chromium layers have been applied by electrodeposition from electrolytes based on hexavalent chromium, which typically comprise chromic acid. The chromium deposits obtained from these electrolytes are essentially pure chromium and have a uniform and invariant colour. A thin oxide layer forms on the top of the coatings giving a blue/white appearance which is very well known. In addition to the incentive to use alternative electrolytes due to serious health and environmental hazards associated with chromic acid, there is also a market demand for coatings having a darker hue.
An initial solution to providing a darker hued deposit from chromium electrolytes can be obtained by electrodepo siting the chromium coatings from electrolytes based on trivaient chromium. Due to the nature of the deposition mechanism from these electrolytes, the chromium coating produced is less pure than that produced from hexavalent electrolytes. This is due to co-deposition of other elements within the coating. Most commonly, these co- deposited elements are iron, sulphur and carbon or combinations thereof. By adjusting the electrolyte formulation of trivaient chromium based processes to maximize the darkness of the deposit produced by the incorporation of these co-deposited elements, coatings of a fairly dark hue can be obtained.
While coatings provided by trivalent chromium electrolytes typically produce darker hued deposits than that of hexavalent chromium electrolytes, the resulting coatings from the prior art are still not dark enough to fulfill the needs of the market and a demand exists to produce darker chromium based coatings. It is the object of this invention to provide a means of producing these coatings.
SUMMARY OF THE INVENTION
It is an object of the invention to provide a trivalent chromium plating electrolyte that is capable of providing dark colored chromium deposits on a substrate.
It is an object of the invention to provide amino acids in the trivalent chromium electrolyte that are capable of creating a dark hue in the resulting trivalent chromium deposit.
It is another object of the invention to provide amino acids in the trivalent chromium electrolyte that have nitrogen containing side chains. It is another object of the invention to provide amino acids that do not contain sulfur in the trivalent chromium electrolyte to provide darker hues of chromium deposits on substrates.
It is yet another object of the invention to provide a darker hued deposit on a substrate using a trivalent chromium electrolyte with select amino acids than the prior art trivalent chromium plating electrolytes can achieve.
It is still another object of the invention to provide a method of plating a trivalent chromium deposit with a dark hue over a nickel deposit.
In one embodiment, a composition is provided for a trivalent chromium electrolyte comprising:
i. trivalent chromium ions,
ii. one or more complexants capable of maintaining the trivalent chromium ions in solution; and
iii. one or more amino acids; wherein the amino acids comprise a cationic side chain comprising nitrogen and wherein the cationic side chain is at least essentially free of sulfur; and
wherein the electrolyte is substantially free of hexavalent chromium salts.
In another embodiment, a method is provided for producing a dark colored chromium deposit on a substrate, comprising the steps of: i. providing a trivalent chromium based electrolyte comprising:
a) trivalent chromium ions,
b) one or more complexants capable of maintaining the trivalent chromium ions in solution, and
c) one or more amino acids,
wherein the amino acids comprise a cationic side chain comprising nitrogen and wherein the cationic side chain is at least essentially free of sulfur; and
wherein the electrolyte is substantially free of hexavalent chromium salts; and
ii, el ectrodepo siting a dark colored chromium deposit on the substrate using the trivalent chromium based electrolyte.
BRIEF DESCRIPTION OF THE DRAWINGS
Figure 1 depicts various classes of amino acids. DETAILED DESCRIPTION OF THE PREFERED EMBODIMENTS
The inventors have surprisingly found that the incorporation of select amino acids which comprise nitrogen containing side chains into the trivalent chromium electrolyte results in coatings which are substantially darker than those obtained from the same electrolyte in the absence of these compounds. The amino acids useful in the current invention are additionally at least essentially free of sulfur. By essentially free of sulfur, it is meant that sulfur is not present in any concentration, aside from trace amounts that may occur as contaminants in such compounds. The darkest coatings are obtained when select amino acids are added to electrolytes which have already been optimised to produce dark coatings by the incorporation of other elements such as sulfur, iron, carbon or combinations thereof.
The use of amino acids as complexants in trivalent chromium plating baths has been described in U.S. Patent No. 4, 107,004 to Ward et al. and U.S. Patent No. 4, 157,945 to Barnes et al., which describe the use of glycine as a complexant. U.S. Patent No. 4, 161,432 to Barclay et al. describes the use of glycine, aspartic acid, arginine and histidine as complexants. U.S. Patent No. 4,448,648 and U.S. Patent No. 4,448,649 both to Barclay et al., describe the use of aspartic acid as a complexant. The subject matter of each of these patents of which is herein incorporated by reference in its entirety. These patents are all focused on producing coatings which are light in color and do not provide for changing the color of the deposit produced or variation of deposit color associated with different amino acids.
Amino acids fall into several groups as shown in Figure 1. The amino acids methionine and cysteine (and cystine) contain bivalent sulphur in their side chains. The use of these sulphur-containing compounds as darkening agents in trivalent chromium baths has been previously disclosed, as for example in WO 2012/150198A1 to Schulz et al., which is hereby incorporated herein by reference in its entirety. This is understood to be a function of the presence of sulfur in the compound, as sulfur is known to cause darker hues in trivalent chromium deposits as compared to the more pure deposits produced from hexavalent chromium electrolytes.
The inventors of the present invention have surprisingly found that sulfur-free amino acids, including those selected from the group having nitrogen containing cationic side chains, have the desired effect of darkening the deposit in a uniform manner. The side chains are cationic under the normal pH conditions of most commercially available trivalent chromium electroplating baths (pH 2.5 - 4.0) due to the presence of a nitrogen-containing (amine) functional group in the side chain.
The amino acids that are useful in the current invention include, for example, arginine, histidine, lysine and combinations thereof. It was found that these amino acids will produce significant darkening of the trivalent chromium deposits. Additionally tryptophan, although not listed under the amino acids containing a positively charged group in Figure 1 , has a nitrogen-containing side chain and is also found to have enhanced darkening effects. From this result, while not wishing to be bound by theory, it is also believed that the side chain of tryptophan is cationic under the normal pH conditions in the trivalent chromium electroplating bath.
The effective concentration range of the preferred amino acids in the trivalent chromium electrolyte is preferably between about 1 g L and about 50 g/1 and more preferably between about 2 g/L and about 20 g 1. The concentration of amino acids in the trivalent chromium electrolyte is most preferably between about 5 g/L and about 10 g/L.
When electroplating from electrolyte solutions described herein, inert anodes, such as carbon anodes, are typically used. Other inert anodes such as platinized titanium, platinum, iridium oxide coated titanium, or tantalum oxide coated titanium may also be used.
The temperature of the trivalent chromium based electrolyte is in the range of 40°C to 60°C, most preferably around 50°C. The pH of the electrolyte is in the range from about 2 to about 5, most preferably about 3.5. The current used during plating is in the range of about 1 amp to about 10 amps, most preferably about 4 amps. Agitation is not required during the plating of substrates in the trivalent chromium electrolyte.
As used herein, the term "about" refers to a measurable value such as a parameter, or a concentration or the like and is meant to include variations of +/- 15% or less, preferably variations of +/- 10% or less, more preferably variations of +/- 5% or less, and most preferably variations of +/- 0.1 % or less from the particularly recited value in so far as such variations are appropriate to carry out the invention as described herein. Furthermore, it is also to be understood that the value to which the modifier "about" refers is itself specifically disclosed herein.
In a preferred embodiment, the substrate comprises nickel deposited on the underlying substrate and the chromium is electroplated on the nickel deposit.
In order to demonstrate the scope of the invention, a Konica Minolta CM2600d spectrophotometer was used to determine the "lightness" values of the various deposits by measuring the L* value according to the L*a*b* colorspace system. The colorspace system gives a quantitative value (L*), which can be used to compare the degree of darkening obtained by the various combinations of amino acid additives. The higher the L* value, the lighter the deposit and the lower the L* value the darker the deposit. An L* value of 0 is black and an L* of 100 is white. Lower L* values are the desire of the current invention.
Dark hued coatings produced by the electrodeposition of trivalent chromium using the electrolytes described herein preferably have an L* value, measured according to an L*a*b* colorspace system, of less than that of typical trivalent chromium deposits that produce light colored coatings and those that have already been maximized for darkness in the resulting deposits.
The trivalent chromium based electrolytes may contain thiocyanate ions. The thiocyanate ions may be present in a concentration anywhere from about 0.2 g/L up to about 5.0 g/L.
The trivalent chromium based electrolytes presented herein are at least substantially free of hexavalent chromium salts, wherein no Cr(VI) ions can be detected in the electrolyte by ordinary measurement techniques.
The trivalent chromium electrolyte comprises a source of trivalent chromium ions, one or more complexants (complexing agents) capable of maintaining the trivalent chromium ions in solution, and the select amino acids as described herein. The amino acids have provided darker hues in the plated deposit compared to the use of the same electrolyte without such amino acids.
The trivalent chromium electrolyte used as a standard is an electrolyte designed to produce light colored chromium deposits. The electrolyte and plating process is based on U.S. Patent No. 4,473,448 to Deeman. This patent is hereby incorporated by reference in its entirety.
Additionally, inventive examples are also provided based on a trivalent chromium electrolyte solution that has already been formulated to produce dark deposits, based on U.S. Patent No. 4, 161 ,432 to Barclay et al. The amino acid used in the electrolyte composition is aspartic acid. This reference is hereby incorporated by reference in its entirety.
The following non-limiting examples illustrate the effectiveness of the invention. All of the examples were prepared by electroplating a trivalent chromium deposit onto Hull cell panels. The Hull Cell panels had previously been electroplated with 10 microns of a bright nickel deposit and are then placed in a Hull Cell with the trivalent chromium electrolyte being tested. For the trivalent chromium plating step, the conditions are as shown in Table 1. Conditions for the trivalent chromium plating remained consistent regardless of the composition being tested.
The lightness or L* value of the trivalent chromium deposit was measured at a point on the Hull Cell panel corresponding to a current density of 8 amps per square decimeter in all cases, which is representative of a normal working range for chromium plating.
Table 1. Trivalent Chromium Platin Hull Cell Conditions
Figure imgf000008_0001
Comparative Example 1
Table 2 provides the L* values measured using the electrolyte based on U.S. Patent No. 4,473,448 to Deeman as a Standard (1 ), with various amino acids added that were not effective darkening agents. Table 2.
Figure imgf000008_0002
Standard (1) plus 5g l Alanine 81.9
Standard (1) plus 5g/l Valine 82.83
Standard (1 ) plus 5g l Isoleucine 82.47
Standard (1) plus 5g/l Proline 82.23
Standard (1) plus 5g/l Phenylalanine 82.25
Standard (1) plus 5g/l Serine 80.7
Standard (1 ) plus 5g/I Threonine 82.78
Standard (1) plus 5 g/1 Tyrosine 83.72
Standard (1) plus 5g l Glutamine 80.51
Standard (1) plus 5g l As artic acid 80.05
As can be seen from the results set forth in Table 2, none of the amino acids tested produced any significant reduction in the L* values when compared to the trivalent chromium electrolyte without amino acids added. The average reduction in L* value was 1 .17%.
Example 1 Table 3 provides the L* values obtained when the amino acids described herein are added to the electrolyte based on U.S. Patent No. 4,473,448 to Deeman. The same Standard (1 ) electrolyte is used as in the comparative example above. As previously noted, this electrolyte typically produces light colored trivalent chromium deposits. Table 3.
Figure imgf000009_0001
In this case, the average reduction in L* value was 12.7% using the examples of the invention of arginine and histidine. This is a significant difference which can easily be seen by eye. The addition of arginine, histidine or lysine gave uniform color across the entire deposit. The addition of tryptophan gave a dramatic effect but produced very uneven and streaky deposits, which although significantly darker, were commercially unacceptable.
Example 2
Table 4 gives the L* values obtained when amino acids of the invention are added to the electrolyte based on U.S. Patent No. 4, 161 ,432 to Barclay et al. This electrolyte was used as the Standard (2) to compare the L* values after the amino acids are added. As previously noted, deposits produced using this electrolyte process were previously formulated to provide dark colored trivalent chromium deposits.
Table 4
Figure imgf000010_0001
In this case, the average reduction in the L* value was 15.02%. This is a very noticeable difference in color. While the electrolyte based on U.S. Patent No. 4,161 ,432 to Barclay et al. naturally produces a dark deposit, it was possible to increase the deposit darkness by the addition of the amino acids as described herein.
As it has been shown by way of the examples presented herein, the inventors have surprisingly found that darker hued deposits can be obtained from trivalent chromium electrolytes that contain the amino acids as described within. The result was unexpected as the effective amino acids did not contain sulfur, but the presence of cationic nitrogen containing side chains allowed for darker hues in the deposits obtained using the trivalent chromium electrolyte of the current invention.
It should also be understood that the following claims are intended to cover all of the generic and specific features of the invention as described herein and all statements of the scope of the invention that as a matter of language might fall there between.

Claims

WHAT IS CLAIMED IS:
1 . A trivalent chromium electrolyte comprising:
i. trivalent chromium ions,
ii. one or more complexants capable of maintaining the trivalent chromium ions in solution; and
iii. one or more amino acids; wherein the amino acids comprise a cationic side chain comprising nitrogen and wherein the cationic side chain is at least essentially free of sulfur; and
wherein the electrolyte is substantially free of hexavalent chromium salts.
2. A trivalent chromium electrolyte according to claim 1, wherein the one or more amino acids are selected from the group consisting of arginine, histidine, lysine, tryptophan, and combinations thereof.
3. A trivalent chromium electrolyte according to claim 1 , wherein the total concentration of amino acids is between about 1 g L and about 50 g/1.
4. A trivalent chromium electrolyte according to claim 3, wherein the total concentration of amino acids is between about 2 g L and about 20 g 1.
5. A trivalent chromium electrolyte according to claim 4, wherein the total concentration of amino acids is between about 5 g L and about 10 g 1.
6. A trivalent chromium electrolyte according to claim 1 , wherein the trivalent chromium plating electrolyte contains thiocyanate ions.
7. The trivalent chromium electrolyte according to claim 6, wherein the thiocyanate ions are present in a concentration between about 0.2 g L and about 5 g/L.
8. The trivalent chromium electrolyte according to claim 2, wherein the amino acid comprises histidine.
9. The trivalent chromium electrolyte according to claim 2, wherein the amino acid comprises arginine.
10. The trivalent chromium electrolyte according to claim 2, wherein the amino acid comprises a mixture of histidine and arginine.
1 1. A method of producing a dark colored chromium deposit on a substrate comprising the steps of: i. providing a trivalent chromium based electrolyte comprising:
a) trivalent chromium ions,
b) one or more complexants capable of maintaining the trivalent chromium ions in solution, and
c) one or more amino acids,
wherein the amino acids comprise a cationic side chain comprising nitrogen and wherein the cationic side chain is at least essentially free of sulfur; and
wherein the electrolyte is substantially free of hexavalent chromium salts; and
ii. electrodepositing a dark colored chromium deposit on the substrate using the trivalent chromium based electrolyte.
12. The method according to claim 1 1 , wherein the one or more amino acids are selected from the group consisting of arginine, histidine, lysine, tryptophan, and combinations thereof.
13. The method according to claim 1 1 , wherein the total concentration of amino acids is between about 1 g/L and about 50 g 1.
14. The method according to claim 13, wherein the total concentration of amino acids is between about 2 g L and about 20 g 1.
15. The method according to claim 14, wherein the total concentration of amino acids is between about 5 g L and about 10 g/1.
16. The method according to claim 1 1 , wherein the trivalent chromium based electrolyte further comprises thiocyanate ions.
17. The method according to claim 16, wherein the thiocyanate ions are present in a concentration between about 0.2 g L and about 5 g L.
18. The method according to claim 12, wherein the one or more amino acids comprises histidine.
19. The method according to claim 12, wherein the one or more amino acid comprises arginine.
20. The method according to claim 12, wherein the one or more amino acids comprises a mixture of histidine and arginine.
21. The method according to claim 1 1, wherein the chromium coating produced on the substrate has an L* value, measured according to an L*a*b!i! colorspace system, lower than the trivalent chromium deposit produced by the same trivalent chromium electrolyte that does not comprise the one or more amino acids.
22. The method according to claim 11, wherein the substrate comprises a nickel deposit on the substrate and the trivalent chromium is plated on the nickel deposit.
23. The method according to claim 1 1 , wherein the pH of the trivalent chromium electrolyte is between about 2.0 and about 5,0.
24. The method according to claim 23, wherein the pH of the trivalent chromium electrolyte is about 3.5.
PCT/US2017/026951 2016-04-21 2017-04-11 Dark colored chromium based electrodeposits Ceased WO2017184380A1 (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
EP17786348.7A EP3443145A4 (en) 2016-04-21 2017-04-11 DARK COLORED CHROME-BASED ELECTRODEPOSITIONS
KR1020187033624A KR20180137531A (en) 2016-04-21 2017-04-11 Dark chrome-based complex
CA3020402A CA3020402A1 (en) 2016-04-21 2017-04-11 Dark colored chromium based electrodeposits
CN201780024363.0A CN109154092A (en) 2016-04-21 2017-04-11 Electrodeposit based on dark chromium
MX2018012675A MX2018012675A (en) 2016-04-21 2017-04-11 Dark colored chromium based electrodeposits.
BR112018071355A BR112018071355A2 (en) 2016-04-21 2017-04-11 dark chrome electrodeposits
JP2018555269A JP2019516016A (en) 2016-04-21 2017-04-11 Dark chrome-based electrodeposition

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US15/134,469 US20170306515A1 (en) 2016-04-21 2016-04-21 Dark Colored Chromium Based Electrodeposits
US15/134,469 2016-04-21

Publications (1)

Publication Number Publication Date
WO2017184380A1 true WO2017184380A1 (en) 2017-10-26

Family

ID=60089417

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US2017/026951 Ceased WO2017184380A1 (en) 2016-04-21 2017-04-11 Dark colored chromium based electrodeposits

Country Status (10)

Country Link
US (1) US20170306515A1 (en)
EP (1) EP3443145A4 (en)
JP (1) JP2019516016A (en)
KR (1) KR20180137531A (en)
CN (1) CN109154092A (en)
BR (1) BR112018071355A2 (en)
CA (1) CA3020402A1 (en)
MX (1) MX2018012675A (en)
TW (1) TWI636161B (en)
WO (1) WO2017184380A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2026012885A2 (en) 2024-07-09 2026-01-15 Macdermid, Incorporated Trivalent chromium plating bath and method of electroplating an article

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2022123008A2 (en) * 2020-12-11 2022-06-16 Atotech Deutschland GmbH & Co. KG Electroplating bath for depositing a black chromium layer, method for depositing, and substrate comprising such a layer
CN116770375B (en) * 2023-06-06 2024-01-02 中山博美新材料科技有限公司 Plating solution for black chromium plating layer, and preparation method and application thereof

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4107004A (en) 1975-03-26 1978-08-15 International Lead Zinc Research Organization, Inc. Trivalent chromium electroplating baths and method
US4157945A (en) 1977-03-04 1979-06-12 International Lead Zinc Research Organization, Inc. Trivalent chromium plating baths
US4161432A (en) 1975-12-03 1979-07-17 International Business Machines Corporation Electroplating chromium and its alloys
US4448649A (en) 1981-11-18 1984-05-15 International Business Machines Corporation Trivalent chromium electroplating baths
US4448648A (en) 1981-11-18 1984-05-15 International Business Machines Corporation Trivalent chromium electroplating baths
US4473448A (en) 1981-02-09 1984-09-25 W. Canning Materials Limited Electrodeposition of chromium
US6004448A (en) * 1995-06-06 1999-12-21 Atotech Usa, Inc. Deposition of chromium oxides from a trivalent chromium solution containing a complexing agent for a buffer
US6468672B1 (en) * 2000-06-29 2002-10-22 Lacks Enterprises, Inc. Decorative chrome electroplate on plastics
WO2012150198A2 (en) 2011-05-03 2012-11-08 Atotech Deutschland Gmbh Electroplating bath and method for producing dark chromium layers

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4062737A (en) * 1974-12-11 1977-12-13 International Business Machines Corporation Electrodeposition of chromium
GB1596995A (en) * 1977-06-14 1981-09-03 Ibm Electroplating chromium and its alloys
KR810001075B1 (en) * 1978-05-31 1981-09-11 제이 에이취 그레이디 "Chrome or Chromium Alloy Electric Plating Solution"
US9765437B2 (en) * 2009-03-24 2017-09-19 Roderick D. Herdman Chromium alloy coating with enhanced resistance to corrosion in calcium chloride environments
US8273235B2 (en) * 2010-11-05 2012-09-25 Roshan V Chapaneri Dark colored chromium based electrodeposits
JP6055611B2 (en) * 2012-05-22 2016-12-27 日本化学工業株式会社 Chrome plating and chrome plating film
US10167564B2 (en) * 2013-01-10 2019-01-01 Coventya, Inc. Apparatus and methods of maintaining trivalent chromium bath plating efficiency

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4107004A (en) 1975-03-26 1978-08-15 International Lead Zinc Research Organization, Inc. Trivalent chromium electroplating baths and method
US4161432A (en) 1975-12-03 1979-07-17 International Business Machines Corporation Electroplating chromium and its alloys
US4157945A (en) 1977-03-04 1979-06-12 International Lead Zinc Research Organization, Inc. Trivalent chromium plating baths
US4473448A (en) 1981-02-09 1984-09-25 W. Canning Materials Limited Electrodeposition of chromium
US4448649A (en) 1981-11-18 1984-05-15 International Business Machines Corporation Trivalent chromium electroplating baths
US4448648A (en) 1981-11-18 1984-05-15 International Business Machines Corporation Trivalent chromium electroplating baths
US6004448A (en) * 1995-06-06 1999-12-21 Atotech Usa, Inc. Deposition of chromium oxides from a trivalent chromium solution containing a complexing agent for a buffer
US6468672B1 (en) * 2000-06-29 2002-10-22 Lacks Enterprises, Inc. Decorative chrome electroplate on plastics
WO2012150198A2 (en) 2011-05-03 2012-11-08 Atotech Deutschland Gmbh Electroplating bath and method for producing dark chromium layers

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of EP3443145A4

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2026012885A2 (en) 2024-07-09 2026-01-15 Macdermid, Incorporated Trivalent chromium plating bath and method of electroplating an article

Also Published As

Publication number Publication date
CN109154092A (en) 2019-01-04
BR112018071355A2 (en) 2019-02-05
KR20180137531A (en) 2018-12-27
US20170306515A1 (en) 2017-10-26
TW201738412A (en) 2017-11-01
MX2018012675A (en) 2019-02-28
EP3443145A4 (en) 2020-01-08
TWI636161B (en) 2018-09-21
JP2019516016A (en) 2019-06-13
EP3443145A1 (en) 2019-02-20
CA3020402A1 (en) 2017-10-26

Similar Documents

Publication Publication Date Title
US8273235B2 (en) Dark colored chromium based electrodeposits
KR101928719B1 (en) Color control of trivalent chromium deposits
WO2017184380A1 (en) Dark colored chromium based electrodeposits
DK151975B (en) CHROME ELECTROPLETING PROCEDURE USING AN AQUILIBRATED Aqueous SOLUTION OF A CHROME (III) THIOCYANATE COMPLEX AS CHROME SOURCE AND CHROMEL ELECTROPLETING SOLUTION USED FOR USE
JP2024520817A (en) Method for controlling the lightness L* of an electroplated chrome layer
CA3155524C (en) Sulfate based, ammonium free trivalent chromium decorative plating process
JP7467758B2 (en) Method for electrodepositing a dark chrome layer on a substrate and substrate completely covered on at least one side with a dark chrome layer
JPS6021235B2 (en) Cobalt-zinc alloy electroplating bath composition and plating method
NO784051L (en) PROCEDURE FOR THE PREPARATION OF SHINES FOR SHINING, GALVANIC ZINC PRECIPITATIONS AND ACID WATER PLATING SOLUTION FOR CARRYING OUT THE PROCEDURE
JP2024520816A (en) Method for electrodepositing a dark chromium layer, substrate containing same, and electroplating bath thereof
KR850000620B1 (en) Chromium Electroplating Solution
Sahrhage Influence of Alloy Composition on Performance of Zinc-Nickel Coatings

Legal Events

Date Code Title Description
ENP Entry into the national phase

Ref document number: 3020402

Country of ref document: CA

ENP Entry into the national phase

Ref document number: 2018555269

Country of ref document: JP

Kind code of ref document: A

NENP Non-entry into the national phase

Ref country code: DE

REG Reference to national code

Ref country code: BR

Ref legal event code: B01A

Ref document number: 112018071355

Country of ref document: BR

WWE Wipo information: entry into national phase

Ref document number: 2017786348

Country of ref document: EP

ENP Entry into the national phase

Ref document number: 20187033624

Country of ref document: KR

Kind code of ref document: A

121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 17786348

Country of ref document: EP

Kind code of ref document: A1

ENP Entry into the national phase

Ref document number: 2017786348

Country of ref document: EP

Effective date: 20181116

ENP Entry into the national phase

Ref document number: 112018071355

Country of ref document: BR

Kind code of ref document: A2

Effective date: 20181017