EP2669407B1 - Galvanic baths for obtaining a low-carat gold alloy, and galvanic process that uses said baths - Google Patents

Galvanic baths for obtaining a low-carat gold alloy, and galvanic process that uses said baths Download PDF

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Publication number
EP2669407B1
EP2669407B1 EP13170067.6A EP13170067A EP2669407B1 EP 2669407 B1 EP2669407 B1 EP 2669407B1 EP 13170067 A EP13170067 A EP 13170067A EP 2669407 B1 EP2669407 B1 EP 2669407B1
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Prior art keywords
salts
galvanic
amounts
gold
baths
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German (de)
French (fr)
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EP2669407A1 (en
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Lorenzo Cavaciocchi
Elena Banchelli
Danilo Vincenzo Canelli
Massimo Innocenti
Ilaria Bencista
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Bluclad SpA
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Bluclad SpA
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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
    • C25D3/56Electroplating: Baths therefor from solutions of alloys
    • C25D3/62Electroplating: Baths therefor from solutions of alloys containing more than 50% by weight of gold
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D7/00Electroplating characterised by the article coated
    • C25D7/005Jewels; Clockworks; Coins

Definitions

  • the invention relates to the field of compounds used in galvanic processes, in particular galvanic baths for obtaining a low-carat gold alloy, and to the galvanic process for obtaining said alloy.
  • Galvanic baths containing considerable amounts of toxic substances, such as cyanides, and heavy metals, which are also toxic and difficult to remove, for example cadmium, in the matrix have been used for decades to obtain a gold alloy containing less than 75% by weight of gold as metal (corresponding to a gold alloy of 18 carats or less).
  • baths of this type also include baths that utilise cyanide in the matrix or that, although they do not contain cyanide in the matrix, contain other doped elements of a certain toxicity.
  • US4358351 describes a bath containing gold, copper, zinc, free cyanide and arsenic as gloss additive
  • US4487664 describes a bath containing gold-silver and free cyanide
  • US5085744 describes a bath containing gold, copper, zinc, free cyanide and antimony as gloss additive
  • US4687557 describes a bath containing gold, copper, and cadmium devoid of free cyanide in solution.
  • WO 2009/037180 describes a gold alloy plating bath comprising gold, copper and indium ions and free cyanide.
  • the present invention makes it possible to satisfy the above-mentioned needs due to alkaline galvanic baths according to claim 1.
  • galvanic bath means the aqueous solutions in which the surfaces to be treated by means of the galvanic process are immersed.
  • the gold salts are preferably selected from: potassium dicyanoaurate, potassium tetracyanoaurate, ammonium cyanoaurate, or a combination thereof.
  • the amount of gold calculated on the basis of the respective salts, is between 0.7 and 4 g/L, preferably between 1.5 and 3 g/L, in order to achieve the desired efficiency and thicknesses.
  • copper salts means, for example: sulfate, phosphate, pyrophosphate, chloride, or other salts that are stable under the working conditions of the bath.
  • Copper calculated on the basis of the respective salts, is present in an amount between 0.3 and 2.5 g/L, preferably between 0.5 and 2 g/L, in relation to the desired carat value in the 12 - 18 carat range.
  • Indium salts useful in accordance with the invention are, for example: chloride, sulfate, citrate, tartrate, gluconate, or any other organic or amine complex compatible with the working conditions of the bath.
  • the concentration of indium ranges from 0.1 to 2 g/L, preferably from 0.5 to 1,5 g/L, in relation to the desired carat value in the 12 - 18 carat range.
  • the matrix of the bath is formed by polycarboxylic acid salts having both buffer characteristics and complexing power, such as citrates, tartrates, gluconates, maleates, malonates, possibly in combination with the corresponding acids for creation of the expedient buffer, and possibly mixed together in order to achieve the expedient complexing power.
  • buffer characteristics and complexing power such as citrates, tartrates, gluconates, maleates, malonates, possibly in combination with the corresponding acids for creation of the expedient buffer, and possibly mixed together in order to achieve the expedient complexing power.
  • These acids and the respective salts are each used in an amount ranging from 30 to 150 g/L, more commonly from 50 to 100 g/L.
  • Complexing agents that can be expediently used in order to improve the stability of the metals in solution and to regulate the properties thereof in alloy include, for example, ethylenediaminetetraacetic acid and salts thereof, etidronic acid and salts thereof, ethylenediamine tetramethyl phosphonic acid and salts thereof, iminodiacetic acid and salts thereof, nitrilotriphosphonic acid and salts thereof, and nitrilotriacetic acid and salts thereof; these complexing agents normally being used in amounts ranging from 1 to 50 g/L according to the complexing power of each one thereof, a person skilled in the art knowing which complexing agent will be the most suitable for use and in what amounts and combinations, according to the desired carat value in the 12 - 18 carat range.
  • a complexing and regulatory action of the alloy metals is due to the amine component of the bath.
  • the amines used for this purpose are triethylenetetramine, diethylenetetramine, ethylenediamine and tetraethylenepentamine.
  • the amine in question is used in amounts ranging from 0.05 to 1 g/L, more expediently from 0.1 to 0.7 g/L, depending on the desired percentage of indium in alloy, within the carat range from 12 to 18 carats.
  • the bath may also obviously contain other components normally used in galvanic processes for their glossing and surfactant action.
  • elements such as silver, tellurium, bismuth, iron, zinc, iridium, rhenium, vanadium, molybdenum, tungsten, in such a form so as to be soluble and stable under the working conditions; the amounts to be used range from 0.005 to 0.2 g/L of element as such, and more in particular from 0.010 to 0.1 g/L.
  • the formulations according to the invention may also comprise sulfurated compounds, such as organic thiols belonging to the classes of mercaptotetrazoles, mercaptopyrimidines, mercaptopyrrols, mercaptoimidazoles and mercaptotriazoles, possibly containing a sulfur atom in the aromatic ring, possibly having a nitrogen ring condensed with a benzene ring, having one or more thio groups.
  • sulfurated compounds such as organic thiols belonging to the classes of mercaptotetrazoles, mercaptopyrimidines, mercaptopyrrols, mercaptoimidazoles and mercaptotriazoles, possibly containing a sulfur atom in the aromatic ring, possibly having a nitrogen ring condensed with a benzene ring, having one or more thio groups.
  • the surfactants have both glossing and surfactant action, and those used normally within galvanic scope in baths having matrices of this type are used in this invention: a person skilled in the art will be able to identify the most suitable type to use; however, the amounts used are never greater than 0.005 L/L of an aqueous solution thereof (10% w/v): higher doses lower the efficiency of the bath and create interference with the regular properties of the metals in alloy.
  • the bath preferably functions in a pH range between 7 and 12, and more expediently between 8 and 10; the pH is regulated with organic acids belonging to the selected buffer pair, or with mineral acids such as sulfuric acid, phosphoric acid, sulfamic acid, methanesulfonic acid, pyridinesulfonic acid, or with alkali metal hydroxides, such as potassium and sodium.
  • organic acids belonging to the selected buffer pair, or with mineral acids such as sulfuric acid, phosphoric acid, sulfamic acid, methanesulfonic acid, pyridinesulfonic acid, or with alkali metal hydroxides, such as potassium and sodium.
  • the pH is not a critical parameter in this formulation for obtaining a precise carat value, but it is fundamental that the pH is alkaline for the stability of the components in solution.
  • the working temperature of the galvanic bath in question is preferably between 50°C and 70°C; however, this is not a critical parameter for obtaining a precise carat value.
  • the current to be applied to the galvanic bath according to the invention is normally between 0.5 - 3 A/cm 2 , preferably 0.7 - 2 A/cm 2 .
  • the application times vary according to the amperage imposed and the desired thickness: with the bath according to the invention, it is possible to obtain deposits having thicknesses up to 500 microns.
  • gold alloys in which the gold varies from 50% to 75% (percentages expressed in weight) are obtained by deposit at the cathode of the galvanic cell.
  • a bath having the following composition was prepared:
  • a current of 0.7 A/cm 2 was applied for 3 minutes to a sheet of nickel-plated brass having a surface area of 0.5 cm 2 , suitably de-greased and re-rinsed with deionised water.
  • the sheet was rinsed with deionised water and dried by compressed air.
  • a bath having the following composition was prepared:
  • the bath was brought to pH 9.5 with potassium hydroxide and heated to 60°C.
  • a current of 1.5 A/cm 2 was applied for 5 minutes to a sheet of nickel-plated brass having a surface area of 0.5 cm 2 , suitably de-greased and re-rinsed with deionised water.
  • the sheet was rinsed with deionised water and dried by compressed air.
  • the surface of the alloy was analysed by electronic scan microscope; the following percentages were found

Description

    Field of the invention
  • The invention relates to the field of compounds used in galvanic processes, in particular galvanic baths for obtaining a low-carat gold alloy, and to the galvanic process for obtaining said alloy.
  • Prior art
  • Galvanic baths containing considerable amounts of toxic substances, such as cyanides, and heavy metals, which are also toxic and difficult to remove, for example cadmium, in the matrix (where matrix means an aqueous solution of organic and inorganic acids and salts thereof) have been used for decades to obtain a gold alloy containing less than 75% by weight of gold as metal (corresponding to a gold alloy of 18 carats or less).
  • These baths make it possible to effectively obtain gold deposits having the desired carat value and considerable thicknesses, however the presence therein of highly poisonous substances makes them virtually unacceptable for practical use.
  • In order to overcome the aforementioned disadvantages, alternatives to the formulations have been sought that in particular would substitute cyanide, as a complexing agent, and cadmium, as a binder, in combination with copper.
  • Previous alternatives in use, however, utilise products that have only partly solved the known problems encountered with the use of the prior galvanic baths and, in addition, do not demonstrate the same suitability for practical use and the same quality of the results: in fact, these are generally formulations which only partly eliminate the toxic products used and which have restricted periods of use or with which an alloy is obtained having characteristics of carat value, thickness or appearance that fail to meet the needs of the intended purpose: in particular, nonuniform deposits or deposits having colourations that are too inclined towards pink and red for the aesthetic purposes for which they are used are obtained.
  • However, baths of this type also include baths that utilise cyanide in the matrix or that, although they do not contain cyanide in the matrix, contain other doped elements of a certain toxicity.
  • For example, US4358351 describes a bath containing gold, copper, zinc, free cyanide and arsenic as gloss additive; US4487664 describes a bath containing gold-silver and free cyanide; US5085744 describes a bath containing gold, copper, zinc, free cyanide and antimony as gloss additive; US4687557 describes a bath containing gold, copper, and cadmium devoid of free cyanide in solution. WO 2009/037180 describes a gold alloy plating bath comprising gold, copper and indium ions and free cyanide.
  • It is therefore obvious in the light of the foregoing that it would be greatly desirable, from the industrial point of view, to make available galvanic baths that are practically free from the above-mentioned toxic substances, are practical in use and make it possible to obtain a precise carat value in the 12 - 18-carat range, suitable thicknesses, uniform deposit and colour tending towards the yellow typical of a gold deposit.
  • Detailed description of the invention
  • The present invention makes it possible to satisfy the above-mentioned needs due to alkaline galvanic baths according to claim 1.
  • In accordance with the present invention, "galvanic bath" means the aqueous solutions in which the surfaces to be treated by means of the galvanic process are immersed.
  • In accordance with the present invention, the gold salts are preferably selected from: potassium dicyanoaurate, potassium tetracyanoaurate, ammonium cyanoaurate, or a combination thereof.
  • It is noted that, by contrast with the above-cited prior art, cyanide is not present in the matrix of the bath in the present invention and its content in the galvanic solution is caused by its counterion function in the gold salts alone and is therefore practically irrelevant, although necessary, for the stability of the gold in solution.
  • The amount of gold, calculated on the basis of the respective salts, is between 0.7 and 4 g/L, preferably between 1.5 and 3 g/L, in order to achieve the desired efficiency and thicknesses.
  • In accordance with the invention, copper salts means, for example: sulfate, phosphate, pyrophosphate, chloride, or other salts that are stable under the working conditions of the bath.
  • Copper, calculated on the basis of the respective salts, is present in an amount between 0.3 and 2.5 g/L, preferably between 0.5 and 2 g/L, in relation to the desired carat value in the 12 - 18 carat range.
  • Indium salts useful in accordance with the invention are, for example: chloride, sulfate, citrate, tartrate, gluconate, or any other organic or amine complex compatible with the working conditions of the bath.
  • The concentration of indium, calculated on the basis of the respective salts, ranges from 0.1 to 2 g/L, preferably from 0.5 to 1,5 g/L, in relation to the desired carat value in the 12 - 18 carat range.
  • The matrix of the bath is formed by polycarboxylic acid salts having both buffer characteristics and complexing power, such as citrates, tartrates, gluconates, maleates, malonates, possibly in combination with the corresponding acids for creation of the expedient buffer, and possibly mixed together in order to achieve the expedient complexing power.
  • These acids and the respective salts are each used in an amount ranging from 30 to 150 g/L, more commonly from 50 to 100 g/L.
  • Complexing agents that can be expediently used in order to improve the stability of the metals in solution and to regulate the properties thereof in alloy include, for example, ethylenediaminetetraacetic acid and salts thereof, etidronic acid and salts thereof, ethylenediamine tetramethyl phosphonic acid and salts thereof, iminodiacetic acid and salts thereof, nitrilotriphosphonic acid and salts thereof, and nitrilotriacetic acid and salts thereof; these complexing agents normally being used in amounts ranging from 1 to 50 g/L according to the complexing power of each one thereof, a person skilled in the art knowing which complexing agent will be the most suitable for use and in what amounts and combinations, according to the desired carat value in the 12 - 18 carat range.
  • A complexing and regulatory action of the alloy metals is due to the amine component of the bath.
  • In particular, it has been found that some types of amine enable finer regulation of the percentage of indium in alloy.
  • In particular, the amines used for this purpose are triethylenetetramine, diethylenetetramine, ethylenediamine and tetraethylenepentamine.
  • The amine in question is used in amounts ranging from 0.05 to 1 g/L, more expediently from 0.1 to 0.7 g/L, depending on the desired percentage of indium in alloy, within the carat range from 12 to 18 carats.
  • The bath may also obviously contain other components normally used in galvanic processes for their glossing and surfactant action.
  • In particular due to the glossing action, it is expedient to add elements, such as silver, tellurium, bismuth, iron, zinc, iridium, rhenium, vanadium, molybdenum, tungsten, in such a form so as to be soluble and stable under the working conditions; the amounts to be used range from 0.005 to 0.2 g/L of element as such, and more in particular from 0.010 to 0.1 g/L.
  • The formulations according to the invention may also comprise sulfurated compounds, such as organic thiols belonging to the classes of mercaptotetrazoles, mercaptopyrimidines, mercaptopyrrols, mercaptoimidazoles and mercaptotriazoles, possibly containing a sulfur atom in the aromatic ring, possibly having a nitrogen ring condensed with a benzene ring, having one or more thio groups.
  • It has been observed that the general effect of these substances is that of regulating the deposition of the gold, improving the uniformity of the deposit and reducing the tendency thereof towards chemical deposition and stain formation.
  • The amounts to be used expediently range from 0.01 to 0.500 g/L, and more in particular from 0.05 to 0.200 g/L.
  • The surfactants have both glossing and surfactant action, and those used normally within galvanic scope in baths having matrices of this type are used in this invention: a person skilled in the art will be able to identify the most suitable type to use; however, the amounts used are never greater than 0.005 L/L of an aqueous solution thereof (10% w/v): higher doses lower the efficiency of the bath and create interference with the regular properties of the metals in alloy.
  • The bath preferably functions in a pH range between 7 and 12, and more expediently between 8 and 10; the pH is regulated with organic acids belonging to the selected buffer pair, or with mineral acids such as sulfuric acid, phosphoric acid, sulfamic acid, methanesulfonic acid, pyridinesulfonic acid, or with alkali metal hydroxides, such as potassium and sodium.
  • The pH is not a critical parameter in this formulation for obtaining a precise carat value, but it is fundamental that the pH is alkaline for the stability of the components in solution.
  • The working temperature of the galvanic bath in question is preferably between 50°C and 70°C; however, this is not a critical parameter for obtaining a precise carat value.
  • The current to be applied to the galvanic bath according to the invention is normally between 0.5 - 3 A/cm2, preferably 0.7 - 2 A/cm2.
  • The application times vary according to the amperage imposed and the desired thickness: with the bath according to the invention, it is possible to obtain deposits having thicknesses up to 500 microns.
  • By expediently varying the applied current, it is possible to obtain alloys of different carat value and colour, since increasing the current applied causes a reduction of the gold in alloy and increases the copper, thus resulting in lower carat values and colours tending more greatly towards red, whereas, vice versa, reducing the current applied causes an increase of the gold in alloy and therefore higher carat values and colours tending more greatly towards yellow.
  • It is therefore possible to achieve any intermediate percentage in the 12 - 18-carat value range in a precise manner by imposing the expedient current.
  • Using the baths as described above, gold alloys in which the gold varies from 50% to 75% (percentages expressed in weight) are obtained by deposit at the cathode of the galvanic cell.
  • Example 1
  • A bath having the following composition was prepared:
    • Citric acid: 50 g/L
    • Potassium citrate: 120 g/L
    • Tetrasodium EDTA: 30 g/L
    • Gold: 1.2 g/L as metal, introduced as potassium dicyanoaurate
    • Copper: 0.7 g/L as metal, introduced as copper sulfate
    • Indium: 0.3 g/L as metal, introduced as indium sulfate
    • Ethylenediamine 0.2 mL/L as pure substance, introduced as aqueous solution 50% w/v
    • Silver 0.05 g/L as metal, introduced as silver cyanide salt 80.6%
    • The bath was brought to pH 8.5 with potassium hydroxide and heated to 60°C.
  • A current of 0.7 A/cm2 was applied for 3 minutes to a sheet of nickel-plated brass having a surface area of 0.5 cm2, suitably de-greased and re-rinsed with deionised water.
  • At the end of the period, the sheet was rinsed with deionised water and dried by compressed air.
  • The colour coordinates measured in accordance with CIELab parameters were as follows: L= 79.2 a= 1.8 b= 13.6
  • Corresponding to an alloy definable as 14 carats.
  • Example 2
  • A bath having the following composition was prepared:
    • Sodium gluconate: 60 g/L
    • Iminodiacetic acid: 80 g/L
    • Gold: 2.5 g/L as metal, introduced as potassium dycanoaurate
    • Copper: 1.8 g/L as metal, introduced as copper sulfate
    • Indium: 0.35 g/L as metal, introduced as indium sulfate
    • Diethylenetetramine 0.1 mL/L as a pure substance, introduced as aqueous solution 50% w/v
    • Rhenium 0.05 g/L as metal, introduced as sodium perrhenate 2-(2-pyrazine)ethane thiol 0.01 g/L as pure substance, introduced in the bath as aqueous solution 10% w/v
  • The bath was brought to pH 9.5 with potassium hydroxide and heated to 60°C.
  • A current of 1.5 A/cm2 was applied for 5 minutes to a sheet of nickel-plated brass having a surface area of 0.5 cm2, suitably de-greased and re-rinsed with deionised water.
  • At the end of the period, the sheet was rinsed with deionised water and dried by compressed air.
  • The colour coordinates measured in accordance with CIELab parameters were as follows: L= 84.8 a= 5.1 b= 16.2
  • The surface of the alloy was analysed by electronic scan microscope; the following percentages were found
    • Au: 74% In: 5% Cu: 22%
    • Corresponding to an alloy definable as 18 carats.

Claims (9)

  1. A galvanic bath comprising aqueous solutions having an alkaline pH and comprising gold salts, copper salts and indium salts, organic polycarboxylic acid salts, organic amines, and possibly complexing agents, sulfurated compounds, surfactants and other metals, wherein the concentration of indium, calculated on the basis of the respective salts, ranges from 0.1 to 2 g/L; wherein said organic amines are selected in the group consisting of triethylenetetramine, diethylenetetramine, ethylenediamine and tetraethylenepentamine; said amines used in amounts ranging from 0.05 to 1 gL; said complexing agent are selected in the group consisting of ethylenediaminetetraacetic acid and salts thereof, etidronic acid and salts thereof, ethylenediamine tetramethyl phosphonic acid and salts thereof, iminodiacetic acid and salts thereof, nitrilotriphosphonic acid and salts thereof, and nitrilotriacetic acid and salts thereof; said sulfurated compounds are selected in the group consisting of organic thiols belonging to the classes of 2-(2-pyrazine)ethane thiol, mercaptotetrazoles, mercaptopyrimidines, mercaptopyrrols, mercaptoimidazoles and mercaptotriazoles, possibly containing a sulfur atom in the aromatic ring, possibly having a nitrogen ring condensed with a benzene ring, having one or more thio groups; said surfactants having both glossing and surfactant action and being those normally used within galvanic baths having matrices formed by said organic polycarboxylic acid salts; said surfactants used in an amount never greater than 0.005 L/L of a 10% w/v aqueous solution thereof; said other metals having glossing action are selected in the group consisting of silver, tellurium, bismuth, iron, zinc, iridium, rhenium, vanadium, molybdenum, tungsten in such a form so as to be soluble and stable under the working conditions in amounts between 0.005 and 0.2 g/L of element as such; said polycarboxylic acid salts having both buffer characteristics and complexing power, possibly in combination with the corresponding acids for creation of the expedient buffer, these acids and the respective salts are each used in an amount ranging from 30 to 150 g/L; characterized in that cyanide is not present in the matrix of the bath and its content in the galvanic solution is caused by its counterion function in the gold salts alone.
  2. The galvanic bath according to claim 1, wherein said gold salts are selected from: potassium dicyanoaurate, potassium tetracyanoaurate, ammonium cyanoaurate, or a combination thereof; said copper salts are selected from: sulfate, phosphate, pyrophosphate, chloride, or other salts that are stable under the working conditions of the bath itself, and said indium salts are selected from chloride, sulfate, citrate, tartrate, gluconate, or an organic or amine complex.
  3. The galvanic bath according to claim 2, wherein the amount of gold ranges from 0.7 to 4 g/L, preferably from 1.5 to 3 g/L, the amount of copper is between 0.3 and 2.5 g/L, preferably between 0.5 and 2 g/L.
  4. The galvanic bath according to any one of claims 1-3, wherein said polycarboxylic acid salts are selected from: citrates, tartrates, maleates, malonates, possibly in combination with the corresponding acids for creation of the suitable buffer, and possibly in a mixture of mixtures thereof, and preferably in amounts between 50 and 100 g/L.
  5. The galvanic bath according to any one of claims 1-4, wherein said amines are triethylenetetramine and diethylenetetramine, preferably in amounts that vary from 0.1 to 0.7 g/L.
  6. The galvanic bath according to any one of claims 1-5, wherein said other metals are used
    in amounts between 0.010 and 0.1 g/L.
  7. Galvanic baths according to claims 1-6, wherein said sulfurated compounds are present in amounts between 0.01 and 0.500 g/L, and more in particular
    in amounts between 0.05 and 0.200 g/L.
  8. Galvanic process for the plating of objects with gold alloys from 12 - 18 carats, wherein the baths according to claims 1 to 7 are used.
  9. Galvanic process according to claim 8, wherein said process is carried out in a pH range between 7 and 12, at a temperature between 50°C and 70°C, and with a current applied between 0.5 - 3 A/cm2.
EP13170067.6A 2012-06-01 2013-05-31 Galvanic baths for obtaining a low-carat gold alloy, and galvanic process that uses said baths Active EP2669407B1 (en)

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IT000103A ITFI20120103A1 (en) 2012-06-01 2012-06-01 GALVANIC BATHROOMS FOR THE ACHIEVEMENT OF A LEAGUE OF LOW-CARATHED GOLD AND GALVANIC PROCESS THAT USES THESE BATHROOMS.

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EP2990507A1 (en) * 2014-08-25 2016-03-02 ATOTECH Deutschland GmbH Composition, use thereof and method for electrodepositing gold containing layers
US20160145756A1 (en) * 2014-11-21 2016-05-26 Rohm And Haas Electronic Materials Llc Environmentally friendly gold electroplating compositions and methods
CN109504991B (en) * 2019-01-21 2020-08-07 南京市产品质量监督检验院 Cyanide-free 18k gold electroforming solution, and preparation method and application thereof

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PT2669407T (en) 2022-06-28
ES2918576T3 (en) 2022-07-19
ITFI20120103A1 (en) 2013-12-02

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