US2783194A - Iodate-containing plating baths - Google Patents

Iodate-containing plating baths Download PDF

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US2783194A
US2783194A US492309A US49230955A US2783194A US 2783194 A US2783194 A US 2783194A US 492309 A US492309 A US 492309A US 49230955 A US49230955 A US 49230955A US 2783194 A US2783194 A US 2783194A
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bath
iodate
plating
cyanide
alkali metal
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US492309A
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Fred I Nobel
Barnet D Ostrow
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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
    • C25D3/46Electroplating: Baths therefor from solutions of silver
    • 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
    • C25D3/38Electroplating: Baths therefor from solutions of copper
    • C25D3/40Electroplating: Baths therefor from solutions of copper from cyanide baths, e.g. with Cu+

Description

IODATE-CONTAINING PLATING BATHS Fred I. Nobel, North Valley Stream, and Barnet D. Ostrow, North Bellmore, N. Y.
No Drawing. Application'March 4, 1955, Serial N0. 492,309
8 Claims. (Cl. 204-46) The'pre'sent invention is directed to electroplating baths, more particularly to the addition to such baths of substances adapted to increase the efiectiveness thereof.
In copper and silver cyanide plating it has been common practice to use sulphur containing additional agents, such as soluble thiocyanates and thiosulphates, in high efiiciency baths. Such agents tend to breakdown during the plating operation, particularly at the higher temperatures used, forming alkali sulphides which narrow the bright plating range and promoting roughness of the deposit. Another undesirable effect of said sulphides was the hardness of the deposit and the difficulty of buifing it. Such sulphides may be brought into the bath incidentally as traces of impurities in the cyanides, in the form of potassium or sodium sulphides.
For example, when sodium thiocyanate is used as a brightener in a bath it breaks down at the high temperature, reacting with alkali metal hydroxide forming alkali metal sulphide and cyanide. In a bath having the following comp:osition z./gal. CuCN 8.0 KCN 12.5 KOH 5.0 NaCNS 2.0
and operated at about 175 F., it will give initially a bright current density range of 0 to 60 amperes persquare foot. After a relatively short time of operation, and due to breakdown of the thiocyanate, the operable bright plating range is reduced to about 0 to 20 amperes per square foot.
In .another type of bright cyanide copper bath compounds of selenium are introduced. These baths are particularly sensitive to the presence of sulphide sulphur. The presence of the traces of sulphides in the cyanides adversely aifects the plating characteristics of such baths. The baths may also be accidentally contaminated by sulphur type compounds, resulting in harmful efiects on the bright plating range. For instance, in a bath of the composition- G./liter Silver (as KAg cyanide) 30 Free KCN 30 K2CO3 30 Selenium (as Na selenite) 5 Na thiosulphate 0.5 Lampon A 1.0
of the prior art, operated at room temperature with cathodic agitation, has .a bright plating range of 0 to 30 amperes per square hoot. After the bath has been in operation for some time, the breakdown of the thiosulphate has an adverse eifect on the deposit in the low current density areas which will become dull, white and smoky. Furthermore, the bright deposit area is narrowed to approximately 20-30 amperes per square foot.
The present invention is intended and adapted to overcome the difliculties and disadvantages inherent in the 2,783,194 Patented Febi26, 1957 prior art, it being among the objects of the invention to provide an addition agent to a plating bath which will sulphate, without affecting the prevent the disturbing effects of sulphide sulphur.
It is also among the objectsof the invention to provide an agent which is intended and adapted to oxidize sulphide sulphur to an innocuous state, such as in the form of cyanide in silver and copper cyanide plating baths. 7
It is further among the objects of the invention to introduce an addition agent into acid nickel plating baths in order to secure smoother and better leveled deposits.
In practicing the present invention, there is added to the bath which may be a copper or silver cyanide bath having a pH of at least 7, a small amount of an alkali metal iodate. Preferably it is in the form of the potassium salt. The specific amount used may be varied within wide limits, and the amount is dependent on the amount of sulphide sulphur to be oxidized by the iodate to the' sulphate. The reaction is probably as follows:
4KIO3+3K2S=3K2SO4+4KI Usually the amount of the alkali metal iodate which is added to the bath is from .001 to 5.0 g./liter of the aqueous solution. I These amounts are usually adequate to take care of the sulphide which is accidentally present or is produced by breakdown of other sulphur compounds.
. of sulphides.
The following are specific examples of the operation of the invention:
Example 1 A bath of the following composition is used wherein the pH is over 13:
Oz./gal. CuCN 8.0 Free KCN 12.5 KOH 5.0 NaCNS 2.0 Cetyl betaine .25
This bath has a bright plating range at the beginning of the plating of O to 60 amperes per square foot. 7 After operation for some time at 170 F. with agitation, the
breakdown of the thiocyanate reduces the bright plating range to 0 to 30 amperes per square foot. With the addition of potassium iodate in the amount of .05 to .2 g./liter, the sulphide is oxidized to sulphate and the original bright plating range is restored.
Example 2 The contamination in this bath comes mainly from sodi-- um sulphide present in the copper cyanide. The bath is operated at F. with agitation. At the beginning of the operation the bath has a bright plating range of 20a to 60 amperes per square foot. l otassiu1n iodate is added in an amount calculated to be sufficient to oxidize the sulphide present, whereby thehright plating range becomes to. 60amperes per square foot.
Example 3 There is provided a bath of a pH of 8.5 having the following constituents:
G./liter CuCN 60 KCN 95 KOH Rochelle salts 45 Selenourea .004
Example 4 A silver cyanide plating bath of the following composition is provided:
G./liter AgCN 30 Total KCN S0 KzCOs 30 KSb tartrate I KzSe -n .001
Plating is conducted at 75 F. with agitation at a bright plating range of 0 to 50 amperes per square foot, which drops to 0 to amperes per square foot in a relatively short time. Upon the addition of sufficient potassium ioda'te to oxidize all of the sulphide sulphur, the original bright plating range is obtained.
Example 5 The silver cyanide bath containing thiosulphate described above wherein after operation the bright plating range has dropped to 20 to amperes per square foot, is treated with an amount of potassium iodate sufiicicnt to oxidize the breakdown products of the thiosulphate. The original bright plating range is restored thereby.
Example 6 Ithas further been found that the addition of the alkali metal iodate has a beneficial effect in the operation of an acid nickel bath, of which the following composition is typical:
G./1iter NiSOiJHsO 300 NiCizJI-IzO HaBOs 52.5 Na naphthaline disulphonate 15 The bath is operated at to F. with agitation. In starting with an article having an R. M. S. of 25 p. in., after depositing .001 inch of nickel from the above bath there is no change in the R. M. S. Then there is added to the bath .12 g./liter of potassium iodate and the article is plated under the same conditions, whereby the R. M. S. is reduced to 15 [.L in.
In the acid nickel plating baths the concentration of the iodate is usually from .05 to 1.0 g./liter with the optimum range of .10 to .50 g./liter. When concentrations greater than 1.0 g./liter are introduced into the bath, there may be developed some adverse eltect on the throwing power of the nickel solution.
We claim:
1. An aqueousmetal plating bath comprising an aqueous alkaline solution of a compound taken from the class consisting of copper cyanide and silver cyanide having incorporated therein an amount sutficient to oxidize sulfide sulfur in said bath of an alkali metal iodate.
2. An aqueous alkaline copper cyanide plating bath having incorporated therein an amount sufiicient to oxidize sulfide sulfur in said bath of sodium iodate.
3. An aqueous alkaline copper cyanide plating bath having incorporated therein an amount sufficient to oxidize sulfide sulfur in said bath of potassium iodate.
4. An aqueous alkaline copper cyanide plating bath having incorporated therein a small amount of an alkali metal iodate in the amount of. .001 to 5.0 g./liter.
5. An aqueous alkaline copper cyanide plating bath having incorporated therein at least .001 gram per liter of an alkali metal iodate.
6. An aqueous alkaline silver cyanide plating bath having incorporated therein at least .001 gram per liter of an alkali metal iodate.
7. An aqueous copper cyanide plating bath containing sulphide sulphur having incorporated therein a sufficient amount of an alkali metal iodate to oxidize said sulphide sulphur.
8. An aqueous silver cyanide plating bath containing sulphide sulphur having incorporated therein a sufficient amount of an alkali metal iodate to oxidize said sulphide sulphur.
References Cited in the file of this patent UNITED STATES PATENTS 1,713,514 Appel May 2l, 1929 OTHER REFERENCES Metal Industry, Nov. 10, 1939, pp. 415-7. American Electroplaters Society (Monthly Review), May 1946, pp. 513-526.

Claims (1)

1. AN AQUEOUS METAL PLATING BATH COMPRISING AN AQUEOUS ALKALINE SOLUTION OF A COMPOND TAKEN FROM THE CLASS CONSISTING OF COPPER CYANIDE AND SILVER CYANIDE HAVING INCORPORATED THEREIN AN AMOUNT SUFFICIENT TO OXIDIZE SULFIDE SULFUR IN SAID BATH OF AN ALKALI METAL IODATE.
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2913376A (en) * 1958-02-20 1959-11-17 Du Pont Process for conditioning copper plating solution
US3322656A (en) * 1962-03-06 1967-05-30 Pittsburgh Plate Glass Co Metal surface of improved bonding quality
US3334031A (en) * 1964-05-18 1967-08-01 Harvest Queen Mill & Elevator High density bipolar electroplating electrolyte
US4153519A (en) * 1976-02-04 1979-05-08 Hitachi, Ltd. Silver-electroplating method using thiocyanic solution

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1713514A (en) * 1926-07-21 1929-05-21 Appel Rudolf Process of electrolytically separating metallic chromium for the production of chromium coatings on other metals

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1713514A (en) * 1926-07-21 1929-05-21 Appel Rudolf Process of electrolytically separating metallic chromium for the production of chromium coatings on other metals

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2913376A (en) * 1958-02-20 1959-11-17 Du Pont Process for conditioning copper plating solution
US3322656A (en) * 1962-03-06 1967-05-30 Pittsburgh Plate Glass Co Metal surface of improved bonding quality
US3334031A (en) * 1964-05-18 1967-08-01 Harvest Queen Mill & Elevator High density bipolar electroplating electrolyte
US4153519A (en) * 1976-02-04 1979-05-08 Hitachi, Ltd. Silver-electroplating method using thiocyanic solution

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