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US3396042A - Chemical gold plating composition - Google Patents

Chemical gold plating composition Download PDF

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Publication number
US3396042A
US3396042A US134106A US13410661A US3396042A US 3396042 A US3396042 A US 3396042A US 134106 A US134106 A US 134106A US 13410661 A US13410661 A US 13410661A US 3396042 A US3396042 A US 3396042A
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US
United States
Prior art keywords
gold
salt
palladous
bath
ions
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Expired - Lifetime
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US134106A
Inventor
Duva Robert
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OMI International Corp
Sel Rex Corp
Original Assignee
Sel Rex Corp
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Filing date
Publication date
Application filed by Sel Rex Corp filed Critical Sel Rex Corp
Priority to US134106A priority Critical patent/US3396042A/en
Priority to GB29612/62A priority patent/GB956922A/en
Priority to CH940562A priority patent/CH405868A/en
Priority to DE19621446259 priority patent/DE1446259B2/en
Publication of US3396042A publication Critical patent/US3396042A/en
Application granted granted Critical
Assigned to OXY METAL INDUSTRIES CORPORATION reassignment OXY METAL INDUSTRIES CORPORATION CHANGE OF NAME (SEE DOCUMENT FOR DETAILS). 4-09-74 Assignors: OXY METAL FINISHING CORPORATION
Assigned to HOOKER CHEMICALS & PLASTICS CORP. reassignment HOOKER CHEMICALS & PLASTICS CORP. MERGER (SEE DOCUMENT FOR DETAILS). Assignors: OXY METAL INDUSTRIES CORPORATION
Assigned to OCCIDENTAL CHEMICAL CORPORATION reassignment OCCIDENTAL CHEMICAL CORPORATION CHANGE OF NAME (SEE DOCUMENT FOR DETAILS). EFFECTIVE MARCH 30, 1982. Assignors: HOOKER CHEMICAS & PLASTICS CORP.
Assigned to OMI INTERNATIONAL CORPORATION reassignment OMI INTERNATIONAL CORPORATION ASSIGNMENT OF ASSIGNORS INTEREST. Assignors: OCCIDENTAL CHEMICAL CORPORATION
Assigned to MANUFACTURERS HANOVER TRUST COMPANY, A CORP OF reassignment MANUFACTURERS HANOVER TRUST COMPANY, A CORP OF SECURITY INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: INTERNATIONAL CORPORATION, A CORP OF DE
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C18/00Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
    • C23C18/16Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
    • C23C18/31Coating with metals
    • C23C18/42Coating with noble metals

Definitions

  • the invention is not limited in scope by explaining a theory upon which the operation is believed to depend. It is believed that when the simpler soluble Pd salts such as palladous chloride or sulfate are employed in the bath of the invention, a complex palladous salt (providing Pd++ ions) is formed in said bath which may be similar in structure to the P salt, for example. In the event that a great excess of free CN ions exists in said bath no deposition takes place. It is believed that this effect is due to the formation of a very stable Pd complex which does not provide Pd ions. The ratio of the Pd salt to free CN- ions should therefore be maintained high enough to provide Pd++ ions which are necessary for the deposition of the gold.
  • aqueous solution consisting essentially of 0.5-30 g./l. of a soluble gold cyanide, 0.01 to 30 g./l. of a soluble palladous salt, absent sufficient CN ions to prevent deposition induced by said palladous salt, and sufficient alkali to provide a pH of 8-11.
  • composition as claimed in claim 2 in which the palladous salt is (NH Pd(NO 5.
  • the composition as claimed in claim 2 in which the palladous salt is disodium palladous tetrachloride.

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  • Chemical & Material Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Chemically Coating (AREA)
  • Electroplating And Plating Baths Therefor (AREA)

Description

United States Patent 3,396,042 CHEMICAL GOLD PLATING COMPOSITION Robert Duva, Paramus, N.J., assignor to Sel-Rex Corporation, Nutley, N.J., a corporation of New Jersey No Drawing. Filed Aug. 28, 1961, Ser. No. 134,106 9 Claims. (Cl. 1061) This invention is concerned with the deposition of gold. More particularly, the invention relates to the deposition of gold without the use of applied current.
The chemical reduction and the immersion deposition of many metals upon basis metals are widely practiced. In the latter process, it is possible to obtain deposit thicknesses of the order of A2 to A of amicron and only on basis metals less noble in the electrolyte than the metal being plated out.
On the other hand, the chemical reduction (electroless) process is not so limited in application as the immersion method, in that the metal will be continually deposited by chemical reduction to substantial thicknesses, although deposition generally is limited to certain catalytic basis metals which effectively accept the deposit. In addition, suitably activated non-conductors can be plated by electroless chemical reduction.
The most common method of electroless chemical reduction employs a solution of the ions of the metal to be deposited and a reducing agent. Most commercial processes employ the hypophosphite ion as the reductant; the bath is operated at about 90 C. and certain buffers are added to prevent wide pH fluctuation. However, gold is a highly electronegative element, i.e., it is easily reduced, and the system containing hypophosphite is unstable with the result that spontaneous decomposition occurs and the bath has to be refined.
This invention is based on the discovery of an entirely different system that will produce gold deposits at the rate of 2 to 2 /2 microns per hour at a temperature substantially below that ordinarily used for either immersion or electroless gold. Furthermore, the bath or baths of the invention are stable for long periods of time under production conditions. Thus, it has been found that gold deposits from a solution thereof in the presence of palladous ions. The palladous ion may be present in the bath containing the gold salt or may be applied to the work to be plated from a separate bath.
The bath of the invention is made up of potassium gold cyanide to which is added 0.01- g./l. of a soluble palladous salt calculated as Pd. Suitable soluble palladous salts include palladium P salt, (NH Pd(NO disodium palladium tetrachloride, Na PdCl palladous chloride and sulfate.
It is to be understood that the invention is not limited in scope by explaining a theory upon which the operation is believed to depend. It is believed that when the simpler soluble Pd salts such as palladous chloride or sulfate are employed in the bath of the invention, a complex palladous salt (providing Pd++ ions) is formed in said bath which may be similar in structure to the P salt, for example. In the event that a great excess of free CN ions exists in said bath no deposition takes place. It is believed that this effect is due to the formation of a very stable Pd complex which does not provide Pd ions. The ratio of the Pd salt to free CN- ions should therefore be maintained high enough to provide Pd++ ions which are necessary for the deposition of the gold. An exact measurement of the working ratio of Pd salt/CN is not possible but it is very simple to test a given solution to see if gold deposits therefrom. It is understood that the palladium of the P salt and of disodium palladium tetrachloride provides Pd++ ions in the gold cyanide bath.
In practicing this invention a bath of the following composition was provided:
As indicated in the broad range of the table above, the alkali salts of weak acids and the weak acid, per se, are optional constituents which, however, improve the stability of the bath. Weak acids are specified because of their buffering and/ or complexing properties. Satisfactory weak acids include the phosphoric acids, and substantially all of the organic acids such as acetic, propionic, kojic, maleic, tartaric, citric, etc. Hydroxy polybasic acids such as citric and polybasic amino acids such as ethylenediamintetraacetic acid (EDTA) are especially desirable because they have a high degree of complexing activity.
The method of plating out the gold is simple in that the bath is heated to about -75 C. and the clean metal workpiece is inserted for sufficient time to obtain the desired thickness of gold.
With the bath comprising 4 g./l. of potassium gold cyanide, 25 g./l. of tripotassium citrate, 12 g./l. of citric acid, 2 g./l. of palladium P salt and sufiicient ammonia to produce a pH of 10, there was obtained a gold thickness of micron in One hour, 2 /2 microns in 2 hours, and 3 /3 microns in three hours. In other experiments satisfactory deposits were obtained at the high and low ranges listed in Table I.
To show that the addition of salts of organic acids are not necessary, a bath was made up as follows:
KAu(CN) 4.0 Palladium P salt 1.5
A copper panel immersed in this bath at 65 C. received a deposit of 18 mg. in 15 minutes, the deposition being matte to semi-bright.
Although satisfactory deposits can be obtained from the basic bath containing only a soluble gold cyanide and palladium P salt, (NI-I Pd(NO the addition of the salts of organic acids such as citric, glycollic, tartaric which are capable of complexing any base metals present in the system and thus maintain the bath in good operating condition for a longer period of time, is very desirable. The sodium salts of citric, glycollic, acetic and tartaric acids have been found to produce satisfactory deposits and to improve the operation of the bath similar to the way the citric acid salt additions do.
As further examples, a bath was made up containing:
G./l. KAu(CN) 4 K HPO 20 Palladium P salt l NH4OH to adjust to pH: 10.0.
G./l. KAU(CN) 4 Na PdCl 1 NH OH to pH 10.
A brass panel immersed in this bath received a gold deposit at the rate of 14 mg./in. in 15 minutes.
The process works as well for a properly sensitized non-conductor. Thus, a printed plastic board with copper circuit elements including holes therein was cleaned, etched in cuprous chloride, treated in 50% HCl, sensitized in stannous chloride solution and then catalyzed by immersing in PdCl solution. The board was then immersed in a solution of 4 g./l. of KAu(CN) 1 g./l. of Na PdCh and 40 g./l. of the disodium salt of EDTA neutralized with NH to pH 10. A satisfactory gold deposit was obtained on the plastic board and through the holes.
The features and principles underlying the invention described above in connection with specific exemplifications will suggest to those skilled in the art many other modifications thereof. It is accordingly desired that the appended claims shall not be limited to any specific feature or details thereof.
I claim:
1. As a composition for chemically depositing gold an aqueous solution consisting essentially of 0.5-30 g./l. of a soluble gold cyanide, 0.01 to 30 g./l. of a soluble palladous salt, absent sufficient CN ions to prevent deposition induced by said palladous salt, and sufficient alkali to provide a pH of 8-11.
2. As a composition for chemically depositing gold, an aqueous solution consisting essentially of Alkali gold cyanide (calc. as Au) 0.5-30 Alkali salt of a weak acid selected from the class consisting of the phosphoric acids and organic acids Up to 300 Weak acid selected from the class consisting of the phosphoric acids and organic acids Up to 100 Palladous salt (calc. as Pd) 0.01-30 Ammonia to pH 8-11.
the CN/Pd++ ratio being below that at which the chemical deposition induced by Pd++ is prevented from taking place by CN ions.
3. As a composition for chemically depositing gold, an aqueous solution containing Potassium gold cyanide About 4. Trialkali citrate About 25. Citric acid About 12. Palladous salt About 2.
Ammonia to approx. pH 10.
the CN/Pd++ ratio being below that at which the chemical deposition induced by Pd++ is prevented from taking place by CN ions.
4. The composition as claimed in claim 2 in which the palladous salt is (NH Pd(NO 5. The composition as claimed in claim 2 in which the palladous salt is disodium palladous tetrachloride.
6. A process for depositing gold on a workpiece having a conducting surface comprising immersing the workpiece in an aqueous solution consisting essentially of 05-30 g./l. of a soluble gold cyanide, sufficient alkali to provide a pH of 8-11, in the presence of 0.01 to 30 g./l. of a soluble palladous salt, and in the absence of sufficient CN ions to prevent deposition induced by said palladous salt whereupon gold is deposited on said conducting surface by the chemical reduction process.
7. A process according to claim 6 wherein the palladous ions are obtained from (NH Pd(NO 8. A process according to claim 6 wherein the palladous ions are obtained from disodium palladium tetrachloride.
9. A process according to claim 6 wherein the palladous ions are obtained from palladous chloride.
JAMES A. SEIDLECK, Primary Examiner.
J. EVANS, Assistant Examiner.

Claims (2)

1. AS A COMPOSITION FOR CHEMICALLY DEPOSITING GOLD AN AQUEOUS SOLUTION CONISTING ESSENTIALLY OF 0.5-30 G./1. OF A SOLUBLE GOLD CYANIDE, 0.01 TO 30 G./1. OF A SOLUBLE PALLADOUS SALT, ABSENT SUFFICIENT CN IONS TO PREVENT DEPOSITION INDUCED BY SAID PALLADOUS SALT, AND SUFFICIENT ALKALI TO PROVIDE A PH OF 8-11.
6. A PROCESS FOR DEPOSITING GOLD ON A WORKPIECE HAVING A CONDUCTING SURFACE COMPRISING IMMERSING THE WORKPIECE IN AN AQUEOUS SOLUTION CONSISTING ESSENTIALLY OF 0.5-30 G./1. OF A SOLUBLE GOLD CYANIDE, SUFFICIENT ALKALI TO PROVIDE A PH OF 8-11, IN THE PRESENCE OF 0.01 TO 30 G./1. OF A SOLUBLE PALLADOUS SALT, AND IN THE ABSENCE OF SUFFICIENT CN IONS TO PREVENT DEPOSITION INDUCED BY SAID PALLADOUS SALT WHEREUPON GOLD IS DEPOSITED ON SAID CONDUCTING SURFACE BY THE CHEMICAL REDUCTION PROCESS.
US134106A 1961-08-28 1961-08-28 Chemical gold plating composition Expired - Lifetime US3396042A (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
US134106A US3396042A (en) 1961-08-28 1961-08-28 Chemical gold plating composition
GB29612/62A GB956922A (en) 1961-08-28 1962-08-01 Chemical gold plating
CH940562A CH405868A (en) 1961-08-28 1962-08-07 Process for plating gold by chemical means and plating composition for the implementation of this process
DE19621446259 DE1446259B2 (en) 1961-08-28 1962-08-28 Aqueous, alkaline gold plating bath

Applications Claiming Priority (1)

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CH (1) CH405868A (en)
DE (1) DE1446259B2 (en)
GB (1) GB956922A (en)

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3468676A (en) * 1963-09-09 1969-09-23 Photocircuits Corp Electroless gold plating
US3607352A (en) * 1968-11-29 1971-09-21 Enthone Electroless metal plating
US3862850A (en) * 1973-06-08 1975-01-28 Ceramic Systems Electroless gold plating on refractory metals
US3993808A (en) * 1971-08-13 1976-11-23 Hitachi, Ltd. Method for electroless plating gold directly on tungsten or molybdenum
US4091128A (en) * 1976-10-08 1978-05-23 Ppg Industries, Inc. Electroless gold plating bath
US4340451A (en) * 1979-12-17 1982-07-20 Bell Telephone Laboratories, Incorporated Method of replenishing gold/in plating baths
US4550036A (en) * 1984-10-18 1985-10-29 Hughes Aircraft Company Electroless silver plating process and system
US4832743A (en) * 1986-12-19 1989-05-23 Lamerie, N.V. Gold plating solutions, creams and baths
US4863766A (en) * 1986-09-02 1989-09-05 General Electric Company Electroless gold plating composition and method for plating
US5178918A (en) * 1986-07-14 1993-01-12 Robert Duva Electroless plating process
US6086946A (en) * 1996-08-08 2000-07-11 International Business Machines Corporation Method for electroless gold deposition in the presence of a palladium seeder and article produced thereby

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2719821A (en) * 1951-07-19 1955-10-04 Charles R Campana Gold alloy plating bath

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2719821A (en) * 1951-07-19 1955-10-04 Charles R Campana Gold alloy plating bath

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3468676A (en) * 1963-09-09 1969-09-23 Photocircuits Corp Electroless gold plating
US3607352A (en) * 1968-11-29 1971-09-21 Enthone Electroless metal plating
US3993808A (en) * 1971-08-13 1976-11-23 Hitachi, Ltd. Method for electroless plating gold directly on tungsten or molybdenum
US3862850A (en) * 1973-06-08 1975-01-28 Ceramic Systems Electroless gold plating on refractory metals
US4091128A (en) * 1976-10-08 1978-05-23 Ppg Industries, Inc. Electroless gold plating bath
US4340451A (en) * 1979-12-17 1982-07-20 Bell Telephone Laboratories, Incorporated Method of replenishing gold/in plating baths
US4550036A (en) * 1984-10-18 1985-10-29 Hughes Aircraft Company Electroless silver plating process and system
US5178918A (en) * 1986-07-14 1993-01-12 Robert Duva Electroless plating process
US4863766A (en) * 1986-09-02 1989-09-05 General Electric Company Electroless gold plating composition and method for plating
US4832743A (en) * 1986-12-19 1989-05-23 Lamerie, N.V. Gold plating solutions, creams and baths
US6086946A (en) * 1996-08-08 2000-07-11 International Business Machines Corporation Method for electroless gold deposition in the presence of a palladium seeder and article produced thereby

Also Published As

Publication number Publication date
DE1446259A1 (en) 1968-11-14
DE1446259B2 (en) 1970-12-17
CH405868A (en) 1966-01-15
GB956922A (en) 1964-04-29

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AS Assignment

Owner name: OXY METAL INDUSTRIES CORPORATION

Free format text: CHANGE OF NAME;ASSIGNOR:OXY METAL FINISHING CORPORATION;REEL/FRAME:003967/0084

Effective date: 19741220

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Owner name: HOOKER CHEMICALS & PLASTICS CORP.

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Effective date: 19801222

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