US3580820A - Palladium-nickel alloy plating bath - Google Patents

Palladium-nickel alloy plating bath Download PDF

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Publication number
US3580820A
US3580820A US695576A US3580820DA US3580820A US 3580820 A US3580820 A US 3580820A US 695576 A US695576 A US 695576A US 3580820D A US3580820D A US 3580820DA US 3580820 A US3580820 A US 3580820A
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United States
Prior art keywords
palladium
nickel
bath
salt
nickel alloy
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Expired - Lifetime
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US695576A
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English (en)
Inventor
Katsumi Yamamura
Shinichi Hayashi
Masao Yamamoto
Yukio Matsubara
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Suwa Seikosha KK
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Suwa Seikosha KK
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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
    • C25D3/567Electroplating: Baths therefor from solutions of alloys containing more than 50% by weight of platinum group metals

Definitions

  • a palladium-nickel alloy plating bath is formed of a solution of palladium salt and a nickel salt in ammonia and a brightener in the nature of a sulfonate or a sulfonamide is added to the bath in which a metal is plated for approximately 30 minutes at a pH in the range of 7.5, temperature in the range of 30 C., and cathode current density in the range of 1 a./dm. without agitation.
  • the present invention relates to a palladium-nickel alloy plating bath.
  • the palladium content in the codeposited layer can be established on any point within the range of 30% and 90% by adjusting the composition of the bath or plating condition, that the so-plated surface obtained shows sufiicient brightness and corrosion-resistance and that accordingly this bath for plating satisfies said object of the invention.
  • the first composition of the bath for plating comprises monosalt such as palladium chloride PdCl and complex salt such as palladous amino chloride Pd(NH Cl are used as supply sources for palladium.
  • monosalt such as palladium chloride PdCl
  • complex salt such as palladous amino chloride Pd(NH Cl) are used as supply sources for palladium.
  • nickel nickel sulfate NiSo -7H O', nickel chloride NiCl '6H O etc. are used.
  • the palladium and nickel salts are converted into the form of amino complex salt.
  • Ammonium salt of inorganic acid or organic acid such as ammonium sulfate and ammonium citrate may be added.
  • a combination of 20 g./l. of palladium and 10 g./l. of nickel produce alloy deposited layer comprising palladium in the amount of and alloy deposited layer composed of 60% of palladium is obtained with a combination of 10 g./l. of palladium and 10 g./l. of nickel. It is not only the concentration ratio of palladium and nickel that afiects the composition of the alloy deposited layer. Nevertheless other conditions such as pH of the bath, the temperature and cathode current density involve negligible problems because it is easy to keep these conditions constant during plating operation and except the pH of the bath the remaining conditions may be relatively varied without adversely affecting the desired results. Therefore desired the codeposited layer can be obtained if essentially the concentration of palladium and nickel in the bath and ratio thereof are controlled within the ranges defined.
  • sulfo compositions such as naphthalenesulfonate or aromatic sulfonamide
  • a bright plating can be obtained.
  • Discovery of these brighteners gave the bath great practical value. Examples of naphthalenesulfonate that can be used are given in the following.
  • aromatic sulionamide examples are:
  • composition and internal stress of the deposited layer show no noticeable change by this bright plating. Satisfactory results can be obtained when said bath is operated at pH 7-10, temperature 15-40 C., cathode current density 0.5-1.5 ampere/dm using palladium or graphite anode.
  • concentration of palladium and nickel must be estimated by chemical analysis and always controlled properly. Supplies of deposition metal is elfectuated by adding said salt directly in the bath. While continuing plating the ammonium salt is gradually accumulated in the bath but it has no deleterious effect.
  • the pH is adjusted by adding ammonia water and dilute sulphuric acid. Generally, lowering of pH tends to enlarge the deposition potential of nickel and increase the nickel content in the deposited layer.
  • palladium content in the deposited layer is not comprised within 30% and 90% owing to improper composition of the bath or plating condition.
  • the palladium content in the codeposited layer goes far from the range of 30 to 90%, solid solution of palladium and nickel is not formed completely and when applied thick plating plated surface loses its brightness and is easy to crack.
  • Other plating conditions are the same with that of conventional method. There are no restriction as to the kind of the base metals.
  • EXAMPLE 1 A bath containing 20 g. of palladous amine chloride Pd(NH Cl 50 cc. of 28% ammonia water and 700 cc. of water was prepared. Then added ammonium sulfate of 50 g., nickel sulfate NiSO -7H O of 50 g. and water sufficient enough to form 1000 cc. of the bath.
  • a brass test piece was plated in said bath for 30 minutes at pH of 7.5, temperature 30 C., cathode current density 1 a./-dm. without agitation.
  • Alloy comprising palladium in 60% and nickel in 40% with white bright surface was obtained from this bath and deposited layer well adhered to the base.
  • EXAMPLE 2 Added 10 g. of sodium 1,3,6-naphthalene trisulfonate to the bath of Example 1, and plated for 30 minutes under the same condition with Example 1.
  • EXAMPLE 3 A bath containing 40 g. of palladous ammine chloride Pd(NH Cl 50 cc. of 28% ammonia water and 700 cc.
  • a brass test piece was plated in said bath for 30 minutes at pH of 8.8, temperature 30 C., cathode current density 1 a./dm. without agitation.
  • a palladium-nickel alloy plating bath having a pH of 7 to 10 composed of ammonia water containing 5 to 30 g./1. of palladium ions, and 5 to 30 g./ l. of nickel ions and an alkali metal naphthalenesulfonate in an amount effective for obtaining a bright palladium-nickel alloy electrodeposited layer in which palladium content is within 30 to thereof.
  • a palladium-nickel alloy plating bath having a pH of 7 to 10 composed of ammonia water containing 5 to 30 g./l. of palladium ions, 5 to 30 g./l. of nickel ions and a member of a group consisting of sodium tit-naphthalenesulfonate, sodium fl-naphthalene-sulfonate, sodium 1,5- naphthalene-disulfonate, and sodium 1,3,6-naphthalenetrisulfonate in an amount effective for obtaining a bright palladium-nickel alloy electrodeposited layer in which palladium content thereof is within 30 to 90%.
  • a palladium-nickel alloy plating bath having a pH of 7 to 10 composed of aqueous ammonia containing in solution a palladium amine complex salt incorporating 5 to 30 g./ 1. of palladium ions, a nickel amine complex salt incorporating 5 to 30 g./l. of nickel ions and, as brightener, an effective amount of sodium 1,3,6-naphthalenetrisulfonate whereby a bright palladium-nickel alloy electrodeposited layer having a palladium content between 30 and 90% may be obtained.
  • a palladium-nickel alloy plating bath having a pH of 7 to 10 composed of aqueous ammonia containing in solution a salt incorporating 5 to 30 g./l. of palladium ions present in the form of palladium-amine chloride and a salt incorporating 5 to 30 g./l.
  • nickel ions present in the form of a member of a group selected from an amine nickel sulphate and an amine nickel chloride and a brightener comprising a member of a group consisting of sodium a-naphthalene-sulfonate, sodium ,B-naphthalene-sulfonate, sodium 1,S-naphthalenedisulfonate, sodium 1,3,6- naphthalene-trisulfonate in an amount effective for obtaining a palladium-nickel alloy electrodeposited layer in which the palladium content is within 30 to 90% thereof.

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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)
US695576A 1967-01-11 1968-01-04 Palladium-nickel alloy plating bath Expired - Lifetime US3580820A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP186867A JPS4733176B1 (enrdf_load_stackoverflow) 1967-01-11 1967-01-11

Publications (1)

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US3580820A true US3580820A (en) 1971-05-25

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US695576A Expired - Lifetime US3580820A (en) 1967-01-11 1968-01-04 Palladium-nickel alloy plating bath
US136588A Expired - Lifetime US3677909A (en) 1967-01-11 1971-04-22 Palladium-nickel alloy plating bath

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US136588A Expired - Lifetime US3677909A (en) 1967-01-11 1971-04-22 Palladium-nickel alloy plating bath

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US (2) US3580820A (enrdf_load_stackoverflow)
JP (1) JPS4733176B1 (enrdf_load_stackoverflow)
GB (1) GB1143178A (enrdf_load_stackoverflow)

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
USB435844I5 (enrdf_load_stackoverflow) * 1974-01-23 1975-01-28
US4098656A (en) * 1976-03-11 1978-07-04 Oxy Metal Industries Corporation Bright palladium electroplating baths
US4100039A (en) * 1976-11-11 1978-07-11 International Business Machines Corporation Method for plating palladium-nickel alloy
US4224115A (en) * 1975-12-03 1980-09-23 Mitsubishi Denki Kabushiki Kaisha Process for forming electrode on semiconductor device
US4297177A (en) * 1980-09-19 1981-10-27 American Chemical & Refining Company Incorporated Method and composition for electrodepositing palladium/nickel alloys
DE3108508A1 (de) * 1981-03-06 1982-09-16 Langbein-Pfanhauser Werke Ag, 4040 Neuss Bad zur galvanischen abscheidung einer palladium/nickel-legierung
US4392921A (en) * 1980-12-17 1983-07-12 Occidental Chemical Corporation Composition and process for electroplating white palladium
US4428802A (en) 1980-09-19 1984-01-31 Kabushiki Kaisha Suwa Seikosha Palladium-nickel alloy electroplating and solutions therefor
DE3400139A1 (de) * 1983-01-07 1984-07-12 Omi International Corp., Warren, Mich. Galvanisches bad fuer die schnellabscheidung von palladium und ein verfahren zur galvanischen schnellabscheidung von palladium
US4487665A (en) * 1980-12-17 1984-12-11 Omi International Corporation Electroplating bath and process for white palladium
US4699697A (en) * 1984-05-24 1987-10-13 Electroplating Engineers Of Japan, Limited High-purity palladium-nickel alloy plating solution and process
US4778574A (en) * 1987-09-14 1988-10-18 American Chemical & Refining Company, Inc. Amine-containing bath for electroplating palladium
US5415685A (en) * 1993-08-16 1995-05-16 Enthone-Omi Inc. Electroplating bath and process for white palladium
US5976344A (en) * 1996-05-10 1999-11-02 Lucent Technologies Inc. Composition for electroplating palladium alloys and electroplating process using that composition
US20090038950A1 (en) * 2007-07-20 2009-02-12 Rohm And Haas Electronic Materials Llc High speed method for plating palladium and palladium alloys
US20110147225A1 (en) * 2007-07-20 2011-06-23 Rohm And Haas Electronic Materials Llc High speed method for plating palladium and palladium alloys

Families Citing this family (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CH572989A5 (enrdf_load_stackoverflow) * 1973-04-27 1976-02-27 Oxy Metal Industries Corp
JPS5254369A (en) * 1975-10-29 1977-05-02 Mitsubishi Electric Corp Schottky barrier semiconductor device
JPS5615656A (en) * 1979-07-18 1981-02-14 Nissan Shoji Kk Preservation of formed rice
JPS5760090A (en) * 1980-09-29 1982-04-10 Nisshin Kasei Kk Supplying method for palladium to palladium-nickel alloy plating solution
DE3108467C2 (de) * 1981-03-06 1983-05-26 Langbein-Pfanhauser Werke Ag, 4040 Neuss Verwendung eines Acetylenamins und/oder eines Aminoalkohols in einem Bad zur galvanischen Abscheidung einer Palladium/Nickel-Legierung
DE3108466C2 (de) * 1981-03-06 1983-05-26 Langbein-Pfanhauser Werke Ag, 4040 Neuss Verwendung eines Acetylenalkohols in einem Bad zur galvanischen Abscheidung einer Palladium/Nickel-Legierung
IT1152087B (it) * 1981-09-11 1986-12-24 Langbein Pfanhauser Werke Ag Procedimento per aumentare la resistenza alla corrosione di una lega palladio-nickel depositata galvanicamente
EP0083488A3 (en) * 1981-12-31 1985-11-06 O'Hara, James Brian Method of producing printed circuits
JPS6051992U (ja) * 1983-09-19 1985-04-12 株式会社 ダイケイ 串刺し米飯加工食品
GB2168381B (en) * 1984-12-12 1988-03-09 Stc Plc Gold plated electrical contacts
US4741818A (en) * 1985-12-12 1988-05-03 Learonal, Inc. Alkaline baths and methods for electrodeposition of palladium and palladium alloys
JPS63110227A (ja) * 1986-10-27 1988-05-14 Sanyo Electric Co Ltd スチロ−ル樹脂成形品
JP6663335B2 (ja) * 2016-10-07 2020-03-11 松田産業株式会社 パラジウム−ニッケル合金皮膜及びその製造方法

Cited By (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
USB435844I5 (enrdf_load_stackoverflow) * 1974-01-23 1975-01-28
US3925170A (en) * 1974-01-23 1975-12-09 American Chem & Refining Co Method and composition for producing bright palladium electrodepositions
US4224115A (en) * 1975-12-03 1980-09-23 Mitsubishi Denki Kabushiki Kaisha Process for forming electrode on semiconductor device
US4098656A (en) * 1976-03-11 1978-07-04 Oxy Metal Industries Corporation Bright palladium electroplating baths
US4100039A (en) * 1976-11-11 1978-07-11 International Business Machines Corporation Method for plating palladium-nickel alloy
US4428802A (en) 1980-09-19 1984-01-31 Kabushiki Kaisha Suwa Seikosha Palladium-nickel alloy electroplating and solutions therefor
US4297177A (en) * 1980-09-19 1981-10-27 American Chemical & Refining Company Incorporated Method and composition for electrodepositing palladium/nickel alloys
US4392921A (en) * 1980-12-17 1983-07-12 Occidental Chemical Corporation Composition and process for electroplating white palladium
US4487665A (en) * 1980-12-17 1984-12-11 Omi International Corporation Electroplating bath and process for white palladium
DE3108508A1 (de) * 1981-03-06 1982-09-16 Langbein-Pfanhauser Werke Ag, 4040 Neuss Bad zur galvanischen abscheidung einer palladium/nickel-legierung
DE3400139A1 (de) * 1983-01-07 1984-07-12 Omi International Corp., Warren, Mich. Galvanisches bad fuer die schnellabscheidung von palladium und ein verfahren zur galvanischen schnellabscheidung von palladium
US4699697A (en) * 1984-05-24 1987-10-13 Electroplating Engineers Of Japan, Limited High-purity palladium-nickel alloy plating solution and process
US4778574A (en) * 1987-09-14 1988-10-18 American Chemical & Refining Company, Inc. Amine-containing bath for electroplating palladium
US5415685A (en) * 1993-08-16 1995-05-16 Enthone-Omi Inc. Electroplating bath and process for white palladium
US5976344A (en) * 1996-05-10 1999-11-02 Lucent Technologies Inc. Composition for electroplating palladium alloys and electroplating process using that composition
US20090038950A1 (en) * 2007-07-20 2009-02-12 Rohm And Haas Electronic Materials Llc High speed method for plating palladium and palladium alloys
US20110147225A1 (en) * 2007-07-20 2011-06-23 Rohm And Haas Electronic Materials Llc High speed method for plating palladium and palladium alloys
US9435046B2 (en) 2007-07-20 2016-09-06 Rohm And Haas Electronics Llc High speed method for plating palladium and palladium alloys

Also Published As

Publication number Publication date
US3677909A (en) 1972-07-18
GB1143178A (en) 1969-02-19
JPS4733176B1 (enrdf_load_stackoverflow) 1972-08-23

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