US2694041A - Electrodeposition of nickel - Google Patents
Electrodeposition of nickel Download PDFInfo
- Publication number
- US2694041A US2694041A US374415A US37441553A US2694041A US 2694041 A US2694041 A US 2694041A US 374415 A US374415 A US 374415A US 37441553 A US37441553 A US 37441553A US 2694041 A US2694041 A US 2694041A
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- nickel
- bath
- liter
- benzene
- sulfonic acid
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D3/00—Electroplating: Baths therefor
- C25D3/02—Electroplating: Baths therefor from solutions
- C25D3/12—Electroplating: Baths therefor from solutions of nickel or cobalt
- C25D3/14—Electroplating: Baths therefor from solutions of nickel or cobalt from baths containing acetylenic or heterocyclic compounds
- C25D3/18—Heterocyclic compounds
Definitions
- This invention relates to-' the electrodeposition of nickel from: an aqueous acidic bath.
- a second and major object is the electrodeposition of brilliant, highly lustrous, ductile nickel plate.
- the first object mentioned above can be accomplished by the addition to the Watts type of nickel bath'or its modifications, of coumarin sulfonic acid,
- the pres-- ence of coumarin sulfonic acid in the bath causes the nickel plate which is electrodeposited therefrom; to be very fine-grained (even though cloudy and milky in appearance), and to show marked increasing luster w1th continued plating, t
- the second object the productionof brilliant, highly lustrous, ductile nickel plate, could be accomplished by the use, in conjunction with the coumarin sulfonic acid, of a material containing another different functional group, vi-z., the unsaturated methylene sulfone group,
- aryl sulfones (sulfonamides, sulfonic acids), in general do not have a critical concentration range in the bath, and they produce practically no further improvement after their optimum concentration is reached.
- coumarin sulfonic acid there is preferential reduction of the unsaturated compound with respect to the nickel ion, whereas with the aryl sulfones, the nickel ion is reduced preferentially.
- the variation of the reduction with the variation of the potentials between adjacent high and low points will account for the rate of brightening or smoothening out eflect.
- the concentration of coumarin sulfonic acid which may be advantageously employed is not critical in any concentration up to saturation: and may be used at concentrations between about 0.5 gram per liter to about 3 grams/liter, the preferred concentration being 0.5 gram/liter to 2.0 grams/ liter.
- the best cathode film buffer is boric acid and it is lmportant to keepits concentration high (over 30 grams/liter), especially in the warm baths.
- Other buffers may be used in small amounts (1 to 5 gram/ liter) with the boric acid with beneficial effects, such as formic, citric, fiuoboric acids, etc., but they are not recommended to be used alone.
- ammonium salts should be kept at a minimum.
- the concentration of zinc and copper ions in the bath should also be kept as low as possible. This is especially desirable where the concentration of aryl sulfones are low in the bath or the latter compounds are absent.
- a simple method for producing the coumarin sulfonic acld which is useful for the purposes of this invention, is to treat coumarin with a minimum of concentrated sulfuric acid to give a clear solution and this clear solution may be added directly to the bath.
- the baths may be operated at pH values ranging from 2.0 to 5.5 and temperatures ranging from 20 C to 70 C. and the preferred current density ranges may be from 5 to amps/sq. ft. depending on the agitat on, the temperature of the bath and the concentration and the type of nickel salts.
- the benzene sulfonamides and sulfonimides may be used effectively in concentrations of from 0.05 gram/liter to saturation.
- a bath for electrodepositing lustrous nickel comprising an aqueous acidic solution consisting essentially of an electrolyte selected from the group consisting of nickel sulfate, nickel chloride and a mixture of nickel sulfate and nickel chloride in the presence of 0.5 to 3.0 grams/liter of coumarin sulfonic acid.
- a method for electrodepositing lustrous nickel consisting of electrodepositing nickel from an aqueous acidic nickel solution consisting essentially of an electrolyte selected from the group consisting of nickel sulfate, nickel chloride and a mixture of nickel sulfate and nickel chloride in the presence of 0.5 to 3.0 grams/liter of coumarin sulfonic acid.
- a method for electrodepositing bright nickel consisting of electrodepositing nickel from an aqueous acidic nickel solution consisting essentially of an electrolyte selected from the group consisting of nickel sulfate, nickel chloride, and a mixture of nickel sulfate and nickel chloride in the presence of an organic compound dissolved in the aqueous acidic nickel solution in a concentration falling within a range of about 0.05 gram/liter to saturation and selected from the group consisting of benzene sulfonamides and sulfonimides, said aqueous acidic nickel solution also having dissolved therein coumarin sulfonic acid in an amount of about 0.5 gram/liter to 3 grams/liter.
- a bath for electrodepositing bright nickel comprising an aqueous acidic solution consisting essentially of an electrolyte selected from the group consisting of nickel sulfate, nickel chloride and a mixture of nickel sulfate and nickel chloride in the presence of an organic compound dissolved in the aqueous acidic nickel solution in a concentration of about 0.05 gram/liter to saturation and selected from the group consisting of benzene sulfonamides and sulfonimides, said aqueous acidic nickel solution also having dissolved therein coumarin sulfonic acid in an amount of about 0.5-3 grams per liter.
Description
2,694,041 nnEcrRonnPostrIoN or NICKEL Henry Brown, Huntington Woods, Mich, assignorto:
Rhea Udylite Corporation, Detroit, Mich., a corporation: of Delaware NoDrawing. Application August14, 1953, b v
Serial No. 374,415
4. Claims. (Cl. 204-49).
This invention relates to-' the electrodeposition of nickel from: an aqueous acidic bath.
' (Dne object of this invention is to decrease the grain size and increasethe luster of. the nickel deposit. v
A second and major object is the electrodeposition of brilliant, highly lustrous, ductile nickel plate.
It has-been found that these. objects can be accomplished by'the use of certain organic compounds.
The first object mentioned above can be accomplished by the addition to the Watts type of nickel bath'or its modifications, of coumarin sulfonic acid, The pres-- ence of coumarin sulfonic acid in the bath causes the nickel plate which is electrodeposited therefrom; to be very fine-grained (even though cloudy and milky in appearance), and to show marked increasing luster w1th continued plating, t
It was further found that the second object, the productionof brilliant, highly lustrous, ductile nickel plate, could be accomplished by the use, in conjunction with the coumarin sulfonic acid, of a material containing another different functional group, vi-z., the unsaturated methylene sulfone group,
as exemplified by benzene sulfonamides and sulfonimides. The presence of coumarin sulfonic acid alone in a Watts type nickel bath or the presence of a material containing the unsaturated methylene sulfone group alone gives no obvious indication of the remarkably diiferent and enhanced result which occurs when both materials are concurrently present.
While the simpler aryl sulfonamides and some of the aryl sulfonic acids produce bright and mirror-like deposits on buffed metals such as bulfed brass, these compounds fail to accomplish the same result on steel which is polished, for example, with 200 emery paper or where the nickel is plated on top of matte (but unburnt) copper plate of 0.003 to 0.0005 thickness, and yield in these cases plate of dull and grey appearance. If, however, coumarin sulfonic acid and a material containing the unsaturated methylene sulfone group are used together, a brilliant mirror-like deposit can be obtained even on a matte copper deposit.
The aryl sulfones (sulfonamides, sulfonic acids), in general do not have a critical concentration range in the bath, and they produce practically no further improvement after their optimum concentration is reached. In the case of coumarin sulfonic acid, there is preferential reduction of the unsaturated compound with respect to the nickel ion, whereas with the aryl sulfones, the nickel ion is reduced preferentially. The variation of the reduction with the variation of the potentials between adjacent high and low points will account for the rate of brightening or smoothening out eflect.
The uniqueness of the aryl sulfones, or broadly the compounds, seems to be mainly tied up with the rate of reduction of the positive valent sulfur compound to negative valent sulfur compound, and the mechanism sulfones.
of its deposition. The fact that with ot-naphthalene sulfonamide as the only-organic compound in the bath, not only isv the odor. of naphthalene apparent. at the: cathode during the plating, but also the analysisof the plate shows the presence of carbon as, well as sulfur and thisv indicates that the mechanism. of the reduction is not of the simplest form.
It is not the sulfone group alone that is responsible. for the eifect of the aryl sulfones because the saturated. alkyl sulfones are not nearly as; effective as the aryl. The benzene and toluene sulfonamides. and ortho benzoyl sulfonimide. are more effective than: aryl. monosulfonic acids, especially of the benzene series, nevertheless, the latter, even though they may not produce bright plate on bulfed' metals, will give brilliant ductile plate when used 'in combination with coumarin sulfonic. acid.
The concentration of coumarin sulfonic acid which may be advantageously employed is not critical in any concentration up to saturation: and may be used at concentrations between about 0.5 gram per liter to about 3 grams/liter, the preferred concentration being 0.5 gram/liter to 2.0 grams/ liter.
ln keepi'ng with their chemical activity, the higher the temperature of' the bath, the more active are the unsaturated groups in the-bath and smaller concentrations' of'compounds carrying them must be used. Furthermore, they function best at the higher pH values of the nickel bath,'that is, 3.0 to 5.2, and their efiectiveness in most cases drops rather suddenly when the pH is lowered past a certain value (in general, at a pH below 3.0 or 2.5-, depending on the type of concentrated compound and on the temperature). The lower the temperature, the higher are the pH values that should be used, and conversely. 1
The best cathode film buffer is boric acid and it is lmportant to keepits concentration high (over 30 grams/liter), especially in the warm baths. Other buffers may be used in small amounts (1 to 5 gram/ liter) with the boric acid with beneficial effects, such as formic, citric, fiuoboric acids, etc., but they are not recommended to be used alone.
In the use of coumarin sulfonic acid alone in the bath, or in the presence of the aryl sulfones, ammonium salts should be kept at a minimum. The concentration of zinc and copper ions in the bath should also be kept as low as possible. This is especially desirable where the concentration of aryl sulfones are low in the bath or the latter compounds are absent. A simple method for producing the coumarin sulfonic acld which is useful for the purposes of this invention, is to treat coumarin with a minimum of concentrated sulfuric acid to give a clear solution and this clear solution may be added directly to the bath.
The baths may be operated at pH values ranging from 2.0 to 5.5 and temperatures ranging from 20 C to 70 C. and the preferred current density ranges may be from 5 to amps/sq. ft. depending on the agitat on, the temperature of the bath and the concentration and the type of nickel salts. The benzene sulfonamides and sulfonimides may be used effectively in concentrations of from 0.05 gram/liter to saturation.
In Table I are listed preferred bath compositions.
In Table II are listed representative examples of the benzene sulfonamides and sulfonimides.
Table II Optimum Benzene Sulfonamides and Sulfonimldes Conn,
grams/liter Benzene sulionamide 0. 1-3 Toluene qnlfnn amides 0, 1-2 o-Benzoyl fimi 0. 1-2 N-Benzoyl benzene sulioninude 0. 1-1 p-Toluene sulphonchloramlde.. 0. 1-1 p-Brom benzene sulionamide 0. 1-1 G-Ohlor o-benzoyl sulfimide. 0. 1-1 M-Aldehydo benzene sulionami 0. 1-1 Sulfomethyl benzene sulfonamlde 0. 1-6 Benzene sulionamlde m-carboxylic amide 0. 1-3 7-Aldehydo o-benzoyl sulflmide 0. 1-3 N-Acetyl benzene sull'onimlde. 0. 1-2 Methoxy benzene sulfonamides 0. 1-1 Hydroxymethyl benzene sulfonamide. 0. 1-2 p-Carboxylic amide benzene sulfonamide 0. 1-3
Table III Preferred formulations for use with the baths of Table I are as follows:
This application is a continuation-in-part of my prior application, Serial No. 749,344, filed May 20, 1947, which was itself a continuation-impart of my prior application, Serial No. 366,385, filed November 20, 1940, both of which are now abandoned.
What is claimed is:
l. A bath for electrodepositing lustrous nickel comprising an aqueous acidic solution consisting essentially of an electrolyte selected from the group consisting of nickel sulfate, nickel chloride and a mixture of nickel sulfate and nickel chloride in the presence of 0.5 to 3.0 grams/liter of coumarin sulfonic acid.
2. A method for electrodepositing lustrous nickel consisting of electrodepositing nickel from an aqueous acidic nickel solution consisting essentially of an electrolyte selected from the group consisting of nickel sulfate, nickel chloride and a mixture of nickel sulfate and nickel chloride in the presence of 0.5 to 3.0 grams/liter of coumarin sulfonic acid.
3. A method for electrodepositing bright nickel consisting of electrodepositing nickel from an aqueous acidic nickel solution consisting essentially of an electrolyte selected from the group consisting of nickel sulfate, nickel chloride, and a mixture of nickel sulfate and nickel chloride in the presence of an organic compound dissolved in the aqueous acidic nickel solution in a concentration falling within a range of about 0.05 gram/liter to saturation and selected from the group consisting of benzene sulfonamides and sulfonimides, said aqueous acidic nickel solution also having dissolved therein coumarin sulfonic acid in an amount of about 0.5 gram/liter to 3 grams/liter.
4. A bath for electrodepositing bright nickel comprising an aqueous acidic solution consisting essentially of an electrolyte selected from the group consisting of nickel sulfate, nickel chloride and a mixture of nickel sulfate and nickel chloride in the presence of an organic compound dissolved in the aqueous acidic nickel solution in a concentration of about 0.05 gram/liter to saturation and selected from the group consisting of benzene sulfonamides and sulfonimides, said aqueous acidic nickel solution also having dissolved therein coumarin sulfonic acid in an amount of about 0.5-3 grams per liter.
References Cited in the file of this patent UNITED STATES PATENTS to 529,825 Great Britain NOV. 28, 1940
Claims (1)
1. A BATH FOR ELECTRODEPOSITING LUSTROUS NICKEL COMPRISING AN AQUEOUS ACIDIC SOLUTION CONSISTING ESSENTIALLY OF AN ELECTROLYTE SELECTED FROM THE GROUP CONSISTING OF NICKEL SULFATE, NICKEL CHLORIDE AND A MIXTURE OF NICKEL SULFATE AND NICKEL CHLORIDE IN THE PRESENCE OF 0.5 TO 3.0 GRAMS/LITER OF COUMARIN SULFONIC ACID.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US374415A US2694041A (en) | 1953-08-14 | 1953-08-14 | Electrodeposition of nickel |
GB23839/54A GB758162A (en) | 1953-08-14 | 1954-08-16 | Improvements in or relating to the electro-deposition of nickel |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US374415A US2694041A (en) | 1953-08-14 | 1953-08-14 | Electrodeposition of nickel |
Publications (1)
Publication Number | Publication Date |
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US2694041A true US2694041A (en) | 1954-11-09 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US374415A Expired - Lifetime US2694041A (en) | 1953-08-14 | 1953-08-14 | Electrodeposition of nickel |
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US (1) | US2694041A (en) |
GB (1) | GB758162A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2840517A (en) * | 1957-07-10 | 1958-06-24 | Rockwell Spring & Axle Co | Nickel-iron-zinc alloy electroplating |
US2900707A (en) * | 1954-08-06 | 1959-08-25 | Udylite Corp | Metallic protective coating |
US2961386A (en) * | 1957-02-21 | 1960-11-22 | Wilmot Breeden Ltd | Electro-deposition of nickel |
US3488264A (en) * | 1965-03-26 | 1970-01-06 | Kewanee Oil Co | High speed electrodeposition of nickel |
US3990955A (en) * | 1974-02-04 | 1976-11-09 | The International Nickel Company, Inc. | Electrodeposition of hard nickel |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2175922B (en) * | 1985-07-03 | 1989-07-05 | Inst Phisikochimia | Nickel sulphamate aqueous electrolyte composition |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB529825A (en) * | 1938-06-15 | 1940-11-28 | Udylite Corp | Improvements in the electrodeposition of nickel |
US2513280A (en) * | 1945-10-31 | 1950-07-04 | Udylite Corp | Electrodeposition of nickel from an acid bath |
US2635076A (en) * | 1947-01-29 | 1953-04-14 | Harshaw Chem Corp | Bright nickel plating |
-
1953
- 1953-08-14 US US374415A patent/US2694041A/en not_active Expired - Lifetime
-
1954
- 1954-08-16 GB GB23839/54A patent/GB758162A/en not_active Expired
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB529825A (en) * | 1938-06-15 | 1940-11-28 | Udylite Corp | Improvements in the electrodeposition of nickel |
US2513280A (en) * | 1945-10-31 | 1950-07-04 | Udylite Corp | Electrodeposition of nickel from an acid bath |
US2635076A (en) * | 1947-01-29 | 1953-04-14 | Harshaw Chem Corp | Bright nickel plating |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2900707A (en) * | 1954-08-06 | 1959-08-25 | Udylite Corp | Metallic protective coating |
US2961386A (en) * | 1957-02-21 | 1960-11-22 | Wilmot Breeden Ltd | Electro-deposition of nickel |
DE1106140B (en) * | 1957-02-21 | 1961-05-04 | Wilmot Breeden Ltd | Acid bath for galvanic deposition of nickel coatings |
US2840517A (en) * | 1957-07-10 | 1958-06-24 | Rockwell Spring & Axle Co | Nickel-iron-zinc alloy electroplating |
US3488264A (en) * | 1965-03-26 | 1970-01-06 | Kewanee Oil Co | High speed electrodeposition of nickel |
US3990955A (en) * | 1974-02-04 | 1976-11-09 | The International Nickel Company, Inc. | Electrodeposition of hard nickel |
Also Published As
Publication number | Publication date |
---|---|
GB758162A (en) | 1956-10-03 |
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