EP2669407A1 - Galvanische Bäder zur Herstellung einer niederkarätigen Goldlegierung und galvanischer Prozess diese Bäder verwendend - Google Patents

Galvanische Bäder zur Herstellung einer niederkarätigen Goldlegierung und galvanischer Prozess diese Bäder verwendend Download PDF

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Publication number
EP2669407A1
EP2669407A1 EP13170067.6A EP13170067A EP2669407A1 EP 2669407 A1 EP2669407 A1 EP 2669407A1 EP 13170067 A EP13170067 A EP 13170067A EP 2669407 A1 EP2669407 A1 EP 2669407A1
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EP
European Patent Office
Prior art keywords
galvanic
salts
gold
baths
bath
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.)
Granted
Application number
EP13170067.6A
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English (en)
French (fr)
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EP2669407B1 (de
Inventor
Lorenzo Cavaciocchi
Elena Banchelli
Vincenzo Danilo Canelli
Massimo Innocenti
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Bluclad SpA
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Bluclad Srl
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Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D3/00Electroplating: Baths therefor
    • C25D3/02Electroplating: Baths therefor from solutions
    • C25D3/56Electroplating: 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).
  • 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.
  • the present invention makes it possible to satisfy the above-mentioned needs due to alkaline galvanic baths containing: gold salts, copper salts and indium salts, organic polycarboxylic acid salts, organic amines, and possibly complexing agents, surfactants and other metals in minor amounts, such as gloss additives and deposit refiners.
  • 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 and diethylenetetramine, but other organic amines, such as ethylenediamine, tetraethylenepentamine and other amines of similar structure, may also perform the same role.
  • 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 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.
  • 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:
  • the bath was brought to pH 8.5 with potassium hydroxide and heated to 60°C.
  • 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 Au: 74% In: 5% Cu: 22% Corresponding to an alloy definable as 18 carats.

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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)
  • Paints Or Removers (AREA)
  • Prevention Of Electric Corrosion (AREA)
EP13170067.6A 2012-06-01 2013-05-31 Galvanische Bäder zur Herstellung einer niederkarätigen Goldlegierung und galvanischer Process verwendent diese Bäder Active EP2669407B1 (de)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
IT000103A ITFI20120103A1 (it) 2012-06-01 2012-06-01 Bagni galvanici per l'ottenimento di una lega di oro a bassa caratura e processo galvanico che utilizza detti bagni.

Publications (2)

Publication Number Publication Date
EP2669407A1 true EP2669407A1 (de) 2013-12-04
EP2669407B1 EP2669407B1 (de) 2022-03-30

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ID=46582807

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EP13170067.6A Active EP2669407B1 (de) 2012-06-01 2013-05-31 Galvanische Bäder zur Herstellung einer niederkarätigen Goldlegierung und galvanischer Process verwendent diese Bäder

Country Status (4)

Country Link
EP (1) EP2669407B1 (de)
ES (1) ES2918576T3 (de)
IT (1) ITFI20120103A1 (de)
PT (1) PT2669407T (de)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2016020812A1 (en) * 2014-08-04 2016-02-11 Nutec International Srl Electrolytic bath, electrolytic deposition method and item obtained with said method
EP2990507A1 (de) * 2014-08-25 2016-03-02 ATOTECH Deutschland GmbH Zusammensetzung, ihre Verwendung und Verfahren zur galvanischen Abscheidung von Gold enthaltenden Schichten
EP3023520A1 (de) * 2014-11-21 2016-05-25 Rohm and Haas Electronic Materials LLC Umweltfreundliche goldelektroplattierungszusammensetzungen und verfahren
CN109504991A (zh) * 2019-01-21 2019-03-22 南京市产品质量监督检验院 一种无氰18k金电铸液、其制备方法及其应用

Citations (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3174918A (en) * 1961-01-24 1965-03-23 Sel Rex Corp Bright gold electroplating
US3878066A (en) * 1972-09-06 1975-04-15 Manfred Dettke Bath for galvanic deposition of gold and gold alloys
US3883409A (en) * 1972-07-10 1975-05-13 Degussa Gold alloy electroplating bath
US4088549A (en) * 1976-04-13 1978-05-09 Oxy Metal Industries Corporation Bright low karat silver gold electroplating
GB2028873A (en) * 1978-08-31 1980-03-12 Lea Ronal Uk Ltd Gold Alloy Electroplating Bath and Method
US4358351A (en) 1980-05-31 1982-11-09 Degussa Aktiengesellschaft Alkaline bath for the electrolytic deposition of low carat yellow colored gold alloy layers
US4487664A (en) 1983-03-16 1984-12-11 Degussa Aktiengesellschaft Method and electrolytic bath for the deposition of low carat bright gold-silver alloy coatings
EP0188386A2 (de) * 1985-01-18 1986-07-23 Engelhard Corporation Gold-Elektroplattierungsbad
US4687557A (en) 1985-03-01 1987-08-18 Heinz Emmenegger Gold alloys and galvanic bath for the electrolytic deposit thereof
US5085744A (en) 1990-11-06 1992-02-04 Learonal, Inc. Electroplated gold-copper-zinc alloys
JP2000319794A (ja) * 1999-04-28 2000-11-21 Seiko Corp めっき皮膜、それを備えた装飾品及びめっき皮膜の製造方法
US6165342A (en) * 1996-07-23 2000-12-26 Degussa Huls Aktiengesellschaft Cyanide-free electroplating bath for the deposition of gold and gold alloys
US20060283714A1 (en) * 2005-06-02 2006-12-21 Rohm And Haas Electronic Materials Llc Gold alloy electrolytes
WO2009037180A1 (fr) * 2007-09-21 2009-03-26 G. Aliprandini Procédé d'obtention d'un dépôt d'alliage d'or jaune par galvanoplastie sans utilisation de métaux ou métalloïdes toxiques
EP2135972A1 (de) * 2007-03-02 2009-12-23 Citizen Tohoku Co., Ltd. Goldlegierungsbeschichtung, mit goldlegierungsbeschichtung umhülltes laminat und mit goldlegierungsbeschichtung umhülltes element

Patent Citations (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3174918A (en) * 1961-01-24 1965-03-23 Sel Rex Corp Bright gold electroplating
US3883409A (en) * 1972-07-10 1975-05-13 Degussa Gold alloy electroplating bath
US3878066A (en) * 1972-09-06 1975-04-15 Manfred Dettke Bath for galvanic deposition of gold and gold alloys
US4088549A (en) * 1976-04-13 1978-05-09 Oxy Metal Industries Corporation Bright low karat silver gold electroplating
GB2028873A (en) * 1978-08-31 1980-03-12 Lea Ronal Uk Ltd Gold Alloy Electroplating Bath and Method
US4358351A (en) 1980-05-31 1982-11-09 Degussa Aktiengesellschaft Alkaline bath for the electrolytic deposition of low carat yellow colored gold alloy layers
US4487664A (en) 1983-03-16 1984-12-11 Degussa Aktiengesellschaft Method and electrolytic bath for the deposition of low carat bright gold-silver alloy coatings
EP0188386A2 (de) * 1985-01-18 1986-07-23 Engelhard Corporation Gold-Elektroplattierungsbad
US4687557A (en) 1985-03-01 1987-08-18 Heinz Emmenegger Gold alloys and galvanic bath for the electrolytic deposit thereof
US5085744A (en) 1990-11-06 1992-02-04 Learonal, Inc. Electroplated gold-copper-zinc alloys
US6165342A (en) * 1996-07-23 2000-12-26 Degussa Huls Aktiengesellschaft Cyanide-free electroplating bath for the deposition of gold and gold alloys
JP2000319794A (ja) * 1999-04-28 2000-11-21 Seiko Corp めっき皮膜、それを備えた装飾品及びめっき皮膜の製造方法
US20060283714A1 (en) * 2005-06-02 2006-12-21 Rohm And Haas Electronic Materials Llc Gold alloy electrolytes
EP2135972A1 (de) * 2007-03-02 2009-12-23 Citizen Tohoku Co., Ltd. Goldlegierungsbeschichtung, mit goldlegierungsbeschichtung umhülltes laminat und mit goldlegierungsbeschichtung umhülltes element
WO2009037180A1 (fr) * 2007-09-21 2009-03-26 G. Aliprandini Procédé d'obtention d'un dépôt d'alliage d'or jaune par galvanoplastie sans utilisation de métaux ou métalloïdes toxiques

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2016020812A1 (en) * 2014-08-04 2016-02-11 Nutec International Srl Electrolytic bath, electrolytic deposition method and item obtained with said method
EP2990507A1 (de) * 2014-08-25 2016-03-02 ATOTECH Deutschland GmbH Zusammensetzung, ihre Verwendung und Verfahren zur galvanischen Abscheidung von Gold enthaltenden Schichten
WO2016030290A1 (en) * 2014-08-25 2016-03-03 Atotech Deutschland Gmbh Composition, use thereof and method for electrodepositing gold containing layers
CN106661751A (zh) * 2014-08-25 2017-05-10 德国艾托特克公司 用于电沉积含金的层的组合物、其用途以及方法
CN106661751B (zh) * 2014-08-25 2019-11-12 德国艾托特克公司 用于电沉积含金的层的组合物、其用途以及方法
EP3023520A1 (de) * 2014-11-21 2016-05-25 Rohm and Haas Electronic Materials LLC Umweltfreundliche goldelektroplattierungszusammensetzungen und verfahren
CN109504991A (zh) * 2019-01-21 2019-03-22 南京市产品质量监督检验院 一种无氰18k金电铸液、其制备方法及其应用

Also Published As

Publication number Publication date
ITFI20120103A1 (it) 2013-12-02
ES2918576T3 (es) 2022-07-19
EP2669407B1 (de) 2022-03-30
PT2669407T (pt) 2022-06-28

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