US3156635A - Gold plating - Google Patents

Gold plating Download PDF

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Publication number
US3156635A
US3156635A US133301A US13330161A US3156635A US 3156635 A US3156635 A US 3156635A US 133301 A US133301 A US 133301A US 13330161 A US13330161 A US 13330161A US 3156635 A US3156635 A US 3156635A
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United States
Prior art keywords
gold
hydrazine
bath
cyanide
alkali
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Expired - Lifetime
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US133301A
Inventor
Foulke Donald Gardner
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Occidental Chemical Corp
Sel Rex Corp
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Sel Rex Corp
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Publication date
Priority to BE620596D priority Critical patent/BE620596A/xx
Application filed by Sel Rex Corp filed Critical Sel Rex Corp
Priority to US133301A priority patent/US3156635A/en
Priority to GB2261/62A priority patent/GB928087A/en
Priority to DES77933A priority patent/DE1215467B/en
Priority to CH872662A priority patent/CH399863A/en
Priority to FR906617A priority patent/FR1331064A/en
Application granted granted Critical
Publication of US3156635A publication Critical patent/US3156635A/en
Anticipated expiration legal-status 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.
Expired - Lifetime 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
    • C25D3/48Electroplating: Baths therefor from solutions of gold

Definitions

  • This invention is based on the discovery that it is possible to obtain 24-carat gold deposits essentially free of organic inclusions by employing a gold bath containing potassium gold cyanide and conducting salts consisting of phosphates or phosphites adjusted to a pH of 36. Gold deposition from such solutions proceeds at an efficiency of less than 100 percent resulting in some loss of hydrogen with the result that the phosphorous acidphosphite solution is somewhat more suitable from a buffer standpoint. Polyphosphoric acids may also be used although they gradually convert to orthophosphate.
  • the deposits obtained from this solution are not bright, being yellow matte to semi-bright, but they are smooth and of high purity.
  • An object of this invention is to provide an acid gold plating bath which is low in organic material so that there is little tendency to codeposit organic compounds with gold.
  • a second object of this invention is to provide a gold plating bath which is low in cyanide, thereby minimizing the tendency to build up a concentration of cyanide break-down products in the bath. Obviously, some alkali cyanide will develop in the bath over a period of time, but at a pH of 36 the concentration is maintained at a low value. However, I have found that the introduction of hydrazine or substituted hydrazines tends to prevent this cyanide build-up and to provide improved electrodeposits.
  • the hydrazine compounds which may be employed are comprised of the water soluble hydrazine salts which is the sulfate, N H .H SO the hydrochloride, N H .2HCl, etc., the water soluble organic hydrazine, hydrazono, and hydrazo compounds, etc. Approximately /2 to 20 g./l. of the hydrazine or hydrazine compound are satisfactory in preventing the build-up of cyanide products.
  • the gold content of the bath is not very critical but very satisfactory deposits are obtained with from 4 to 36 g./l. of soluble gold salt.
  • the phosphate or phosphite anions are present in the bath in the proportion of about 5 to 200 g./l.
  • the phosphate and phosphate anions may be added to the bath as acids in which case, the pH is adjusted to the range of 36 by the addition of alkali.
  • Example 1 A bath of the following composition was prepared:
  • Example 2 A bath was made up as follows:
  • Brass panels plated in this bath were similar in appearance to those obtained from the phosphoric acid phosphate bath.
  • the addition of methyl hydrazine in one case and dimethyl hydrazine in another case gave brighter deposits.
  • Potassium phosphite could be substituted for the equivalent amount of KOH and phosphorous acid to make this bath.
  • Example 3 A bath was made up according to Example 1, except that only 2 g./l. of gold (as sodium gold cyanide) were added. Satisfactory deposits were obtained up to 0.6 amp/dm. Increasing the phosphate content to 200 g./l. had no observable effect on the deposit, but the voltage drop across the cell was lowered.
  • gold sodium gold cyanide
  • Example 4 A bath was prepared as follows:
  • a plating solution for plating approximately 24k 15 selected from the group consisting of phosphoric, phosphorous and polyphosphoric acid anions,
  • a plating solution as claimed in claim 4 comprising 1 to 10 g./l. of hydrazine sulfate.

Description

United States Patent 3,156,635 GOLD PLATING Donald Gardner Foullre, Watchung, Piainfield, N.J., assignor to Sci-Rex Corporation, Nutley, N.J., a corporation of New Jersey N0 Drawing. Filed Aug. 23, 1%1, Ser. No. 133,301 Claims. (Cl. 20446) This invention is concerned with the deposition of gold and specifically with the deposition of gold from a bath relatively free of organic compounds, resulting in minimum codeposition of organic materials with the gold.
From the early beginning of gold plating until very recently gold plating has been done from a cyanide electrolyte almost exclusively. Some plating was done from the acid trivalent gold complex, HAuCl but this solution is highly corrosive and not at all suitable for production work. More recently gold has been plated from a bath on the acid side of the pH range, pH 3.5-6.0, to which was added considerable amounts of organic acids and their salts. Although this formulation circumvented the ageold problem of eliminating the build-up of undesirable cyanide decomposition products characteristic of the conventional hot cyanide gold baths, obviously considerable organic material is present in the solution, some of which may co-deposit with the gold.
This invention is based on the discovery that it is possible to obtain 24-carat gold deposits essentially free of organic inclusions by employing a gold bath containing potassium gold cyanide and conducting salts consisting of phosphates or phosphites adjusted to a pH of 36. Gold deposition from such solutions proceeds at an efficiency of less than 100 percent resulting in some loss of hydrogen with the result that the phosphorous acidphosphite solution is somewhat more suitable from a buffer standpoint. Polyphosphoric acids may also be used although they gradually convert to orthophosphate.
The deposits obtained from this solution are not bright, being yellow matte to semi-bright, but they are smooth and of high purity.
An object of this invention, therefore, is to provide an acid gold plating bath which is low in organic material so that there is little tendency to codeposit organic compounds with gold.
A second object of this invention is to provide a gold plating bath which is low in cyanide, thereby minimizing the tendency to build up a concentration of cyanide break-down products in the bath. Obviously, some alkali cyanide will develop in the bath over a period of time, but at a pH of 36 the concentration is maintained at a low value. However, I have found that the introduction of hydrazine or substituted hydrazines tends to prevent this cyanide build-up and to provide improved electrodeposits.
The hydrazine compounds which may be employed are comprised of the water soluble hydrazine salts which is the sulfate, N H .H SO the hydrochloride, N H .2HCl, etc., the water soluble organic hydrazine, hydrazono, and hydrazo compounds, etc. Approximately /2 to 20 g./l. of the hydrazine or hydrazine compound are satisfactory in preventing the build-up of cyanide products.
The gold content of the bath is not very critical but very satisfactory deposits are obtained with from 4 to 36 g./l. of soluble gold salt.
3,156,635 Patented Nov. 10, 1964 ice The phosphate or phosphite anions are present in the bath in the proportion of about 5 to 200 g./l. The phosphate and phosphate anions, may be added to the bath as acids in which case, the pH is adjusted to the range of 36 by the addition of alkali.
Examples of the method of carrying out this invention are as follows:
Example 1 A bath of the following composition was prepared:
KAu(CN) 12 KH PQ, 30
dm. The efficiency was 120 mg./ amp minute.
Example 2 A bath was made up as follows:
KAu(CN) g./l 12 Phosphorous acid (30%) ml 200 KOH to pH=3.5.
Brass panels plated in this bath were similar in appearance to those obtained from the phosphoric acid phosphate bath. The addition of methyl hydrazine in one case and dimethyl hydrazine in another case gave brighter deposits. Potassium phosphite could be substituted for the equivalent amount of KOH and phosphorous acid to make this bath.
Example 3 A bath was made up according to Example 1, except that only 2 g./l. of gold (as sodium gold cyanide) were added. Satisfactory deposits were obtained up to 0.6 amp/dm. Increasing the phosphate content to 200 g./l. had no observable effect on the deposit, but the voltage drop across the cell was lowered.
Example 4 A bath was prepared as follows:
G./l. KAu(CN) 12 Polyphosphoric acid KOH to pH=3.5.
Deposits similar to those in Examples 1 and 2 were obtained, except the deposits were brighter. Increasing the gold to 24 g./l. extended the permissible current density range upwards, at a pH of 6.0 the deposits continued to be ductile and were somewhat brighter.
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. The method of electrodepositing gold which coma prises electrolyzing an aqueous solution containing an alkali metal gold cyanide in the amount of 4 g./l. to 36 g./l., a nitrogen compound selected from the group consisting of hydrazine, water soluble substituted hydrazine compounds and salts of hydrazine, and a combination of acidic anions selected from the group consisting of phosphoric, phosphorous and polyphosphoric acid anions and sufiicient alkali to give a pH of 3.0-6.0.
2. The process as claimed in claim 1 in which the acid anion is phOSphate anion and is present in the proportion of about 5 to 200 g./l.
3. The process as claimed in claim 1 in which the acid anion is phosphite anion and is present in the proportion of about 5 to 200 g./l.
4. A plating solution for plating approximately 24k 15 selected from the group consisting of phosphoric, phosphorous and polyphosphoric acid anions,
sufficient alkali to provide a pH of 3 to 6 and an amount up to about 20 g./l. of a hydrazine compound selected from the group consisting of hydrazine, hydrazine salts and Water soluble substitution products of hydrazine. 5. A plating solution as claimed in claim 4 comprising 1 to 10 g./l. of hydrazine sulfate.
References Cited in the file of this patent UNITED STATES PATENTS 2,176,668 Egeberg et a1 Oct. 17, 1939 2,654,702 De Long Oct. 6, 1953 2,812,299 Volk Nov, 5, 1957 2,978,390 Atwater et al Apr. 4, 1961

Claims (1)

1. THE METHOD OF ELECTRODEPOSITING GOLD WHICH COMPRISES ELECTROLYZING AN AQUEOUS SOLUTION CONTAINING AN ALKALI METRAL GOLD CYANIDE IN THE AMOUNT OF 4 G/1 TO 36 G./L., A NITROGEN COMPOUND SELECTED FROM THE GROUP CONSISTING OF HYDRAZINE, WATER SOLUBLE SUBSITUTED HYDRAZINE COMPOUNDS AND SALTS OF HYDRAZINE, AND A COMBINATION OF ACIDIC ANIONS SELECTED FROM THE GROUP CONSISTING OF PHOSPHORIC, PHOSPHOROUS AND POLYPHOSPHORIC ACID ANIONS AND SUFFICIENT ALKALI TO GIVE A PH OF 3.0-6.0
US133301A 1961-08-23 1961-08-23 Gold plating Expired - Lifetime US3156635A (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
BE620596D BE620596A (en) 1961-08-23
US133301A US3156635A (en) 1961-08-23 1961-08-23 Gold plating
GB2261/62A GB928087A (en) 1961-08-23 1962-01-22 Gold plating
DES77933A DE1215467B (en) 1961-08-23 1962-02-07 Bath for the galvanic deposition of 24 carat gold coatings
CH872662A CH399863A (en) 1961-08-23 1962-07-19 Process for the electrolytic deposition of gold and electrolyte for the implementation of this process
FR906617A FR1331064A (en) 1961-08-23 1962-08-09 Process for the electrolytic deposition of gold and electrolyte for the implementation of this process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US133301A US3156635A (en) 1961-08-23 1961-08-23 Gold plating

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US133301A Expired - Lifetime US3156635A (en) 1961-08-23 1961-08-23 Gold plating

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BE (1) BE620596A (en)
CH (1) CH399863A (en)
DE (1) DE1215467B (en)
GB (1) GB928087A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3445352A (en) * 1966-09-23 1969-05-20 Western Electric Co Gold electroplating process and solution
DE2001497B2 (en) 1969-01-15 1973-01-04 Pmd Chemicals Ltd., Coventry, Warwickshire (Grossbritannien) Process for the production of an aqueous, galvanic gold bath

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4207149A (en) * 1974-12-04 1980-06-10 Engelhard Minerals & Chemicals Corporation Gold electroplating solutions and processes

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2176668A (en) * 1938-02-10 1939-10-17 Int Silver Co Silver plating process
US2654702A (en) * 1948-09-03 1953-10-06 Dow Chemical Co Electrodepostion of metal from alkaline cyanide bath
US2812299A (en) * 1949-05-05 1957-11-05 Birle & Co K G Electrolytic deposition of gold and gold alloys
US2978390A (en) * 1957-07-22 1961-04-04 Bell Telephone Labor Inc Gold plating solutions

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2176668A (en) * 1938-02-10 1939-10-17 Int Silver Co Silver plating process
US2654702A (en) * 1948-09-03 1953-10-06 Dow Chemical Co Electrodepostion of metal from alkaline cyanide bath
US2812299A (en) * 1949-05-05 1957-11-05 Birle & Co K G Electrolytic deposition of gold and gold alloys
US2978390A (en) * 1957-07-22 1961-04-04 Bell Telephone Labor Inc Gold plating solutions

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3445352A (en) * 1966-09-23 1969-05-20 Western Electric Co Gold electroplating process and solution
DE2001497B2 (en) 1969-01-15 1973-01-04 Pmd Chemicals Ltd., Coventry, Warwickshire (Grossbritannien) Process for the production of an aqueous, galvanic gold bath

Also Published As

Publication number Publication date
GB928087A (en) 1963-06-06
BE620596A (en)
CH399863A (en) 1965-09-30
DE1215467B (en) 1966-04-28

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Owner name: OXY METAL INDUSTRIES CORPORATION

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

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Owner name: HOOKER CHEMICALS & PLASTICS CORP.

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