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US20060137991A1 - Method for bronze galvanic coating - Google Patents

Method for bronze galvanic coating Download PDF

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Publication number
US20060137991A1
US20060137991A1 US10/531,142 US53114205A US2006137991A1 US 20060137991 A1 US20060137991 A1 US 20060137991A1 US 53114205 A US53114205 A US 53114205A US 2006137991 A1 US2006137991 A1 US 2006137991A1
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US
United States
Prior art keywords
electrolyte
concentration
wetting agent
tin
aromatic
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.)
Abandoned
Application number
US10/531,142
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English (en)
Inventor
Katrin Zschintzsch
Joachim Heyer
Marlies Kleinfeld
Stefan Schafer
Ortrud Steinius
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 Enthone Inc
Original Assignee
Enthone 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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=32010957&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=US20060137991(A1) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Enthone Inc filed Critical Enthone Inc
Assigned to ENTHONE INC. reassignment ENTHONE INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: STEINIUS, ORTRUD, HEYER, JOACHIM, KLEINFELD, MARLIES, SCHAFER, STEFAN, ZSCHINTZSCH, KATRIN
Publication of US20060137991A1 publication Critical patent/US20060137991A1/en
Abandoned legal-status Critical Current

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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
    • C25D3/58Electroplating: Baths therefor from solutions of alloys containing more than 50% by weight of copper
    • 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
    • C25D3/60Electroplating: Baths therefor from solutions of alloys containing more than 50% by weight of tin

Definitions

  • This invention concerns a method for electrodeposition of bronzes, with which the substrate to be coated is plated in an acid electrolyte that contains at least tin and copper ions, an alkylsulfonic acid and a wetting agent, and the preparation of such an electrolyte.
  • acid electrolytes and methods for deposition of qualitatively high grade tin or tin alloys with a higher deposition rate are known from EP 1 111 097 A2 and U.S. Pat. No. 6,176,996 B1. These are electrolytes that contain at least two divalent metal salts of an organic sulfonic acid and from which are deposited solderable and corrosion resistant coatings that can be used, for example, as substitutes for lead-containing solderable coatings in electronics for manufacture of circuit boards, etc.
  • bronze coatings are used in the jewelry industry as a substitute for expensive silver or allergy-triggering nickel.
  • methods for electrodeposition of bronzes are also gaining importance in some technical fields, for example in electronics for coating electronic components or in mechanical engineering and/or in process technology for coating bearing overlays and friction layers.
  • chiefly white bronzes or the so-called “false bronzes,” whose copper content can be kept quite low due to process conditions, are deposited as nickel substitutes.
  • the invention is based on the task of providing a method for deposition of bronzes that, in contrast to the methods known from the prior art, enables uniform deposition of at least tin and copper side by side from an acid electrolyte at considerably higher deposition rates. Moreover, with this method firmly bonding and pore-free bronze coatings with high copper contents as well as various decorative and mechanical properties are said to be deposited.
  • an acid electrolyte that can have a high content of divalent copper ions, is stable with respect to oxidation-caused sludge formation, and is both economical and environmentally friendly when used over a long period of time, is to be made available.
  • the task is solved in accordance with the invention by a method of the kind mentioned at the start, which is characterized by the fact that an aromatic, nonionic wetting agent is added to the electrolyte.
  • a method for electrodeposition of bronzes is made available, where an anode of a copper-tin alloy and a cathode are connected to the substrate that is to be coated by means of an electrolyte, and coating takes place by passing a direct current through them.
  • an electrolyte that is usable in particular for this method and the coatings that are obtainable by this method are made available.
  • the disadvantages known in the prior art are remedied with the offering of a new electrolyte composition and in this way considerably better deposition results are achieved.
  • the conduct of the method is made to be simpler and more economical.
  • This, too, is chiefly based on the advantageous composition of the electrolyte.
  • the method is carried out at room temperature, or between 17 and 25° C., and the substrate to be coated is plated in a highly acid environment at a pH ⁇ 1.
  • the electrolyte is particularly stable in this temperature range.
  • there are no longer any costs for heating the electrolyte and the plated substrates also do not have to be cooled very much, with large expenditures of time and money.
  • deposition rates of 0.25 im/min at a current density of 1 A/dm 2 are achieved due to, among other things, the pH value and the advantageous addition of at least one aromatic non-ionic wetting agent.
  • this rate can be raised up to 7 A/dm 2 in rack operation and even up to 120 A/dm 2 for continuous plants.
  • usable current densities in a range from 0.1-120 A/dm 2 are reached in each case according to plant type.
  • the wetting of the surfaces to be plated is considerably improved in particular through the addition of at least one aromatic nonionic wetting agent to the electrolyte.
  • Another advantage of the aromatic nonionic wetting agent that is used is that because of the advantageous wetting properties the electrolyte and/or the substrate in the electrolyte need to be agitated only a little or even not at all, in order to achieve the desired deposition results, so that additional devices for agitation of the electrolyte can be omitted.
  • electrolyte residues drain from the plated substrate better when it is removed from the electrolyte, which leads to reduced entrainment losses and thus to lower process costs.
  • the proposed method is therefore advantageously economical and environmentally friendly compared to the cyanide processes.
  • anionic and/or aliphatic nonionic wetting agent that is known from the prior art is also optionally possible, provided these wetting agents support or even enhance the advantageous effects of the aromatic nonionic wetting agent.
  • polyethylene glycols and/or anionic surfactants are preferably added to the electrolyte as anionic and/or aliphatic nonionic wetting agents.
  • the method in accordance with the invention is characterized in particular by the special composition of the electrolyte. It contains essentially tin and copper ions, an alkylsulfonic acid and an aromatic nonionic wetting agent.
  • stabilizers and/or complexing agents, anionic and/or nonionic, aliphatic wetting agents, oxidation inhibitors, brighteners, and other metal salts can optionally be contained in the electrolyte.
  • Tin methanesulfonate is especially preferably used as tin salt in the electrolyte preferably in an amount of 5-195 g/L of electrolyte, preferably 11-175 g/L of electrolyte. This corresponds to a use of 2-75 g/L, preferably 4-57 g/L divalent tin ions.
  • Copper methanesulfonate is especially preferably used in the electrolyte as the copper salt, which is advantageously added to the electrolyte in an amount of 8-280 g/L of electrolyte, preferably 16-260 g/L of electrolyte. This corresponds to the use of 2-70 g/L, preferably 4-65 g/L divalent copper ions.
  • an acid preferably a mineral and/or an alkylsulfonic acid
  • an acid is added to the electrolyte in amounts of 140-382 g/L of electrolyte, preferably 175-245 g/L of electrolyte.
  • methanesulfonic acid turned out to be especially advantageous, since for one thing this produces advantageous solubility of metal salts and for another, because of its acid strength, it produces or facilitates the adjustment of the pH needed for the process.
  • methanesulfonic acid has the advantageous property of contributing considerably to the stability of the bath.
  • At least one additional metal and/or chloride is added to the electrolyte.
  • the metals are in the form of their soluble salts.
  • the addition of zinc and/or bismuth has a considerable effect on the properties of the deposited coatings.
  • the metals zinc and/or bismuth added to the electrolyte can namely be in the form of salts of alkylsulfonic acids, preferably as methanesulfonates or as salts of mineral acids, preferably as sulfates.
  • Zinc sulfate is especially preferably uses in the electrolytes as zinc salt, and is advantageously added in an amount of 0-25 g/L of electrolyte, preferably 15-20 g/L of electrolyte.
  • Bismuth methane sulfate is especially preferably used in the electrolyte as bismuth salt and is advantageously added to the electrolyte in an amount of 0-5 g/L of electrolyte, preferably 0.05-0.2 g/L of electrolyte.
  • additives for example stabilizers and/or complexing agents, oxidation inhibitors and brighteners, that are usually used in acid electrolytes for deposition of tin alloys can be added to the electrolyte.
  • Gluconates are advantageously added to the electrolyte and stabilizers and/or complexing agents.
  • the concentration of the stabilizers and/or complexing agents is 0-50 g/L of electrolyte, preferably 20-30 g/L of electrolyte.
  • Compounds from the class of the dihydroxybenzenes, for example mono- or polyhydroxyphenyl compounds like pyrocatechol or phenolsulfonic acid are preferably used as oxidation inhibitors.
  • the concentration of oxidation inhibitors is 0-5 g/L of electrolyte.
  • the electrolyte contains hydroquinone as oxidation inhibitor.
  • the conduct of the method in accordance with the invention enables the deposition of bronzes onto various substrates.
  • all of the usual methods for making electronic components can be used.
  • especially hard and wear-resistant bronze coatings can be deposited on materials like bearings, etc., to the method in accordance with the invention.
  • the method in accordance with the invention is advantageously also used in the fields of decorative coating of, for example, fixtures and jewelry, etc., where the deposition of multi-component alloys that contain tin, copper, zinc and bismuth is particularly advantageous in these areas.
  • a really special advantage is that the so-called “true” bronzes that have a copper content >60% can be deposited with the method in accordance with the invention, where the copper content can be up to 95 wt % in each according to the desired properties.
  • the ratio of the amount of copper to the amount of tin in the electrolyte has a considerable effect of properties like hardness and color of the bronze coatings. For instance, at a tin/copper ratio of 40/60 silver-colored coatings, the so-called white bronzes, which are relatively soft, are deposited. At a tin/copper ratio of 20/80 yellow gold colored coatings result, the so-called yellow bronzes, and at a tin/copper ratio of 10/90 red gold colored coatings are formed, the so-called red bronzes.
  • the electrolyte contains brighteners from the class of the aromatic carbonyl compounds and/or á,â-unsaturated carbonyl compounds.
  • the concentration of brighteners is 0-5 g/L of electrolyte.
  • the base electrolyte of the highly acid electrolyte in accordance with the invention contains essentially (per liter of electrolyte)
  • electrolyte per liter of electrolyte
  • the electrolyte is prepared by varying the individual components, as given below as a matter of example. Additional information about the corresponding process conditions as well as other properties of the individual coatings can be seen in Table 1.
  • Coating/Amounts Example in wt % Properties of coating No. Sn Cu Zn Bi Hardness Ductility Gloss Color 1 10 90 — — 180 HV 50 ++ Yes Red 2a 20 80 — — 283 Hv 50 ⁇ Yes Yellow 2b 20 80 — — 317 HV 50 ⁇ Yes Yellow 3 40 60 — — 360 HV 50 ⁇ Yes White 4 90 10 — — — ⁇ No White 5 20 80 ⁇ 1 — — +++ Yes Yellow 6 20 80 — ⁇ 1 345 HV 50 ⁇ Yes Yellow 7 20 80 ⁇ 1 — — ++ Yes Yellow

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)
  • Chemically Coating (AREA)
  • Electroplating Methods And Accessories (AREA)
US10/531,142 2002-10-11 2003-10-10 Method for bronze galvanic coating Abandoned US20060137991A1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
EP02022718.7A EP1408141B1 (fr) 2002-10-11 2002-10-11 Methode et électrolyte pour la deposition galvanique des bronzes
EP020227187 2002-10-11
PCT/EP2003/011229 WO2004035875A2 (fr) 2002-10-11 2003-10-10 Procede de depot galvanique de bronzes

Publications (1)

Publication Number Publication Date
US20060137991A1 true US20060137991A1 (en) 2006-06-29

Family

ID=32010957

Family Applications (1)

Application Number Title Priority Date Filing Date
US10/531,142 Abandoned US20060137991A1 (en) 2002-10-11 2003-10-10 Method for bronze galvanic coating

Country Status (7)

Country Link
US (1) US20060137991A1 (fr)
EP (1) EP1408141B1 (fr)
JP (1) JP4675626B2 (fr)
KR (1) KR100684818B1 (fr)
CN (1) CN1703540B (fr)
ES (1) ES2531163T3 (fr)
WO (1) WO2004035875A2 (fr)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20050263403A1 (en) * 2002-10-11 2005-12-01 Enthone Inc. Method for electrodeposition of bronzes
EP2071057A2 (fr) 2007-12-12 2009-06-17 Rohm and Haas Electronic Materials LLC Bronze d'électrodéposition
US20090205714A1 (en) * 2006-05-24 2009-08-20 Kuehnlein Holger Metal Plating Composition and Method for the Deposition of Copper-Zinc-Tin Suitable for Manufacturing Thin Film Solar Cell
US20110089043A1 (en) * 2008-05-08 2011-04-21 Umicore Galvanotechnik Gmbh Modified copper-tin electrolyte and process for the deposition of bronze layers
US20110174631A1 (en) * 2008-07-10 2011-07-21 Umicore Galvanotechnik Gmbh Copper-tin electrolyte and process for the deposition of bronze layers
US8426241B2 (en) 2010-09-09 2013-04-23 International Business Machines Corporation Structure and method of fabricating a CZTS photovoltaic device by electrodeposition
US9145617B2 (en) 2011-08-30 2015-09-29 Rohm And Haas Electronic Materials Llc Adhesion promotion of cyanide-free white bronze
US20200071140A1 (en) * 2018-09-05 2020-03-05 Vis, Llc Power unit for a floor jack

Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102004041701A1 (de) * 2004-08-28 2006-03-02 Enthone Inc., West Haven Verfahren zur elektrolytischen Abscheidung von Metallen
WO2006036479A1 (fr) * 2004-09-24 2006-04-06 Jarden Zinc Products, Inc. Metaux deposes par electrodeposition presentant un aspect blanc argente et procede de production
US7296370B2 (en) * 2004-09-24 2007-11-20 Jarden Zinc Products, Inc. Electroplated metals with silvery-white appearance and method of making
CN100368924C (zh) * 2005-05-31 2008-02-13 西北工业大学 一种非周期性红外波段负磁导率材料
ES2698205T5 (en) 2005-11-25 2025-02-27 Macdermid Enthone Inc Process for cleaning of processing solutions
ATE453740T1 (de) 2007-02-14 2010-01-15 Umicore Galvanotechnik Gmbh Kupfer-zinn-elektrolyt und verfahren zur abscheidung von bronzeschichten
DE102011008836B4 (de) * 2010-08-17 2013-01-10 Umicore Galvanotechnik Gmbh Elektrolyt und Verfahren zur Abscheidung von Kupfer-Zinn-Legierungsschichten
CN102605394B (zh) * 2012-03-07 2015-02-18 深圳市华傲创表面技术有限公司 一种无氰酸性白铜锡电镀液
JP6101510B2 (ja) * 2013-02-18 2017-03-22 株式会社シミズ 非シアン銅−錫合金めっき浴
CA2957587C (fr) * 2014-08-08 2019-03-05 Okuno Chemical Industries Co., Ltd. Bain de placage d'alliage de cuivre-etain
US11597637B2 (en) 2018-02-22 2023-03-07 Vis, Llc Under hoist support stand
EP3540097A1 (fr) 2018-03-13 2019-09-18 COVENTYA S.p.A. Produits galvanisés et bain électrolytique approprié pour fournir de tels produits

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US4565608A (en) * 1983-11-02 1986-01-21 Degussa Aktiengesellschaft Alkaline cyanide bath for electrolytic deposition of copper-tin-alloy coatings
US5176957A (en) * 1989-12-05 1993-01-05 Sumitomo Rubber Industries, Ltd. Bead wire for tire, rubber-coated bead wire for tire and tire using the same
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US5443714A (en) * 1989-10-19 1995-08-22 Blasberg Oberflachentechnik, Gmbh Process and electrolyte for depositing lead and lead-containing layers
US5494565A (en) * 1993-01-27 1996-02-27 Degussa Aktiengesellschaft Method of producing workpieces of non-corrosion-resistant metals with wear-resistant coatings and articles
US6176996B1 (en) * 1997-10-30 2001-01-23 Sungsoo Moon Tin alloy plating compositions
US6372117B1 (en) * 1999-12-22 2002-04-16 Nippon Macdermid Co., Ltd. Bright tin-copper alloy electroplating solution
US6458284B1 (en) * 1999-08-20 2002-10-01 Mitsubishi Denki Kabushiki Kaisha Method of etching and etch mask
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US2854388A (en) * 1955-03-14 1958-09-30 City Auto Stamping Co Electrodeposition of copper-tin alloys
US4565608A (en) * 1983-11-02 1986-01-21 Degussa Aktiengesellschaft Alkaline cyanide bath for electrolytic deposition of copper-tin-alloy coatings
US5443714A (en) * 1989-10-19 1995-08-22 Blasberg Oberflachentechnik, Gmbh Process and electrolyte for depositing lead and lead-containing layers
US5176957A (en) * 1989-12-05 1993-01-05 Sumitomo Rubber Industries, Ltd. Bead wire for tire, rubber-coated bead wire for tire and tire using the same
US5494565A (en) * 1993-01-27 1996-02-27 Degussa Aktiengesellschaft Method of producing workpieces of non-corrosion-resistant metals with wear-resistant coatings and articles
US5385661A (en) * 1993-09-17 1995-01-31 International Business Machines Corporation Acid electrolyte solution and process for the electrodeposition of copper-rich alloys exploiting the phenomenon of underpotential deposition
US6176996B1 (en) * 1997-10-30 2001-01-23 Sungsoo Moon Tin alloy plating compositions
US6508927B2 (en) * 1998-11-05 2003-01-21 C. Uyemura & Co., Ltd. Tin-copper alloy electroplating bath
US6458284B1 (en) * 1999-08-20 2002-10-01 Mitsubishi Denki Kabushiki Kaisha Method of etching and etch mask
US6607653B1 (en) * 1999-09-27 2003-08-19 Daiwa Fine Chemicals Co., Ltd. Plating bath and process for depositing alloy containing tin and copper
US6372117B1 (en) * 1999-12-22 2002-04-16 Nippon Macdermid Co., Ltd. Bright tin-copper alloy electroplating solution
US20040035714A1 (en) * 2000-09-20 2004-02-26 Michael Dietterle Electrolyte and method for depositing tin-copper alloy layers
US7179362B2 (en) * 2000-09-20 2007-02-20 Dr.-Ing. Max Schlotter Gmbh & Co.Kg Electrolyte and method for depositing tin-copper alloy layers
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Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20050263403A1 (en) * 2002-10-11 2005-12-01 Enthone Inc. Method for electrodeposition of bronzes
US20060260948A2 (en) * 2005-04-14 2006-11-23 Enthone Inc. Method for electrodeposition of bronzes
US9263609B2 (en) 2006-05-24 2016-02-16 Atotech Deutschland Gmbh Metal plating composition and method for the deposition of copper—zinc—tin suitable for manufacturing thin film solar cell
US20090205714A1 (en) * 2006-05-24 2009-08-20 Kuehnlein Holger Metal Plating Composition and Method for the Deposition of Copper-Zinc-Tin Suitable for Manufacturing Thin Film Solar Cell
EP2071057A2 (fr) 2007-12-12 2009-06-17 Rohm and Haas Electronic Materials LLC Bronze d'électrodéposition
US20110089043A1 (en) * 2008-05-08 2011-04-21 Umicore Galvanotechnik Gmbh Modified copper-tin electrolyte and process for the deposition of bronze layers
US20110174631A1 (en) * 2008-07-10 2011-07-21 Umicore Galvanotechnik Gmbh Copper-tin electrolyte and process for the deposition of bronze layers
US8426241B2 (en) 2010-09-09 2013-04-23 International Business Machines Corporation Structure and method of fabricating a CZTS photovoltaic device by electrodeposition
US9041141B2 (en) 2010-09-09 2015-05-26 International Business Machines Corporation Structure and method of fabricating a CZTS photovoltaic device by electrodeposition
US8790956B2 (en) 2010-09-09 2014-07-29 International Business Machines Corporation Structure and method of fabricating a CZTS photovoltaic device by electrodeposition
US9145617B2 (en) 2011-08-30 2015-09-29 Rohm And Haas Electronic Materials Llc Adhesion promotion of cyanide-free white bronze
US20200071140A1 (en) * 2018-09-05 2020-03-05 Vis, Llc Power unit for a floor jack
WO2020050961A1 (fr) * 2018-09-05 2020-03-12 Vis, Llc Unité d'énergie pour un cric rouleur
US10906789B2 (en) * 2018-09-05 2021-02-02 Vis, Llc Power unit for a floor jack

Also Published As

Publication number Publication date
JP2005537394A (ja) 2005-12-08
ES2531163T3 (es) 2015-03-11
KR100684818B1 (ko) 2007-02-22
EP1408141B1 (fr) 2014-12-17
JP4675626B2 (ja) 2011-04-27
EP1408141A1 (fr) 2004-04-14
WO2004035875A3 (fr) 2005-04-14
CN1703540B (zh) 2010-10-06
WO2004035875A2 (fr) 2004-04-29
KR20050059174A (ko) 2005-06-17
CN1703540A (zh) 2005-11-30

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