US2147415A - Electroplating - Google Patents
Electroplating Download PDFInfo
- Publication number
- US2147415A US2147415A US141972A US14197237A US2147415A US 2147415 A US2147415 A US 2147415A US 141972 A US141972 A US 141972A US 14197237 A US14197237 A US 14197237A US 2147415 A US2147415 A US 2147415A
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- plating
- alcohol
- bath
- foaming
- per liter
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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
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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)
Description
Patented Feb. E4, 1939 Nil) STATES PATENT, oF'FicE Eastman Kodak Company, Rochester,
N. Y., a
corporation of New Jersey No Drawing. Application May 11, 1937,, Serial No. 141,972
Z Claims.
This invention relates to electroplating and more particularly to a method for preventing foaming of anti-pitting agents of the surface tension lowering type in plating operations wherein the article being plated is agitated, or the solution is agitated by the frequent removal of the articles being plated.
Heretofore, it has been found in electroplating articles in plating solutions with metals such as cobalt, copper, nickel, lead, iron, zinc, etc., that a great improvement in the metal plating can be produced by adding anti-pitting agents of the surface tension lowering type to the plating baths.
When employed in non-agitated plating solutions this type of anti-pitting agent, among the best of which are higher sulphonated alcohols, perform very satisfactorily. However, when such higher sulphonated alcohols are employed in plating solutions in which the article being plated (the cathode) is removed frequently, or rotated partly immersed, trouble is experienced with foaming of the solution which frequently overflows the plating bath and seriously interferes with the plating operation.
An object of the invention is therefore a process by which higher sulphonated alcohol antipitting agents may be employed in electroplating solutions without excessive foaming.
Another object of the invention is a non-foaming plating solution containing anti-pitting" agents or other addition agents which have a tendency to foam excessively particularly when agitated.
In accordance with the invention these and other objects are attained by adding to a suitable electroplating solution containing non-pitting agents such as sulphonated alcohols, or other surface tension lowering substances, a small percent of insoluble higher aliphatic alcohols.
I have found that the aliphatic alcohols and theirisomers from 051111011 to C1oHz1OH inclusively are particularly valuable as foam preventing agents for use in electroplating baths containing non-pitting agents such as higher sulphonated alcohols. Of these octyl alcohol, CaI-InOH, is especially useful. These materials do not interfere with the plating operation as do oils and are therefore particularly adaptable for use in electroplating solutions where it is necessary that the cathode be frequently removed or rotated partly immersed.
Suitable higher sulphonated alcohols and other sulphonated substances suitable for use as antipitting agents which without the addition of allphatic alcohols will cause excessive foaming when used in agitated plating solutions are: alkyl sulphonic acids such as lauryl sulphonic acid, and salts of alkyl sulphonic acids such as sodium lauryl sulphonate and sodium palmatyl sulphonate; aromatic sulphonic acids such as benzene sulphonic acid and aryl sulphonic acid salts such as benzene sodium sulphonate, and naphthalenic sulphonic acids and salts thereof such as sodium naphthyl sulphonate. I have also found that the anti-pitting agent available on the market under the trade name Harshaw Non-Fitting Agent and also the nonpitting or wetting agents known as Du Ponal", Igepon T and Daconal, (all of which I believe to be higher sulphonated alcohols or mixtures containing sulphonated alcohols) will foam excessively when employed in acid plating-solutions when the solution is agitated as heretofore described, and that the addition of a small amount of insoluble aliphatic alcohols and their isomers within the group comprising C5H11OHtOC1oH21OH inclusive to the plating solution will prevent excessive foaming of such anti-pitting agents without perceptibly changing the plating characteristics of the plating solution and, in fact, improving the action of the anti-pitting agents.
The following are examples of non-foaming electrolytic baths suitable for plating nickel on an article which is rotated at comparatively high speeds while partially immersed in the solution:
Example 1 NiSO4-7H2O 140 g/l NiC12-6H2O 40 g/l II3BO3 40 g/l sulphonated higher alcohol (CnH2n-' ISH) 3 g/l Octyl alcohol (CaHmOl-l) '4g/1 ExampleZ I NiSO4-7H2O 140 g/l 40 NiClz-GHzO 40 g/l HsBOs 40 g/l Harshaw non-pitting agent 25 00/1 Octyl alcohol (CaHnOH) 4g/l Example 3 NiSO4-7H2O 140 g/l NiC12-6H2O 40 g/l H3303 40 g/l Du Ponal 3 g/l Octyl alcohol, (CsHi'zOH) 4 g/l While the preferred amounts of the contents of the electroplating bath are given in the above examples, the content of NiSO4 may be Within the range of 100-300 grams per liter, the Nick .be-;
tween 20-100 grams per liter, the H3BO3 between 15-40 grams per liter, the sulphonated higher alcohols or Du Ponal between 1-20 grams per liter, the octyl alcohol between 2-10 grams per liter, and the Harshaw non-pitting agent in Example 2 between 10-40 cc. per liter, and a. good plating without foaming may be obtained.
The following are examples of non-foaming electrolytic baths suitable for plating copper on an article which is rotated at comparatively high speeds while partially immersed in the solution: Example 4 CLISO45H2O 200 g/l H2804 70 g/l sulphonated higher alcohol (CnH2n-1SH) 3 g/l Octyl alcohol (CaHnOH) 4g/l Example 5 CuSo4-5H2O 200 g/l H2804 70 g/l Harshaw non-pitting agent 25 cc/] Octyl alcohol (CaHnOH) Example 6 01180451120 200 g/l H2804 '70 g/l Duponal 3 g/l Octyl alcohol (CsHnOH) 4g/l In addition to the specific amounts employed in the above examples of copper plating solutions, satisfactory plating without foaming may be obtained when the bath contains CuSO4 in the range of 100-300 grams per liter, H2804 from 3 to grams per liter sulphonated higher alcohol Duponal 1-20 grams per liter, octyl alcohol 2-10 grams per liter and in the case of Example 5, Harshaw non-pitting agent 10-40 cc. per liter.
The above examples are given for purposes of illustration and are not limitations of the invention. I have found that the addition of one or more of the aliphatic alcohols and their isomers from C5H11OH to C10H21OH in amount within the range of from 0.2% to 10% and preferably within a range of 0.2% to 1% based on the amount of foam producing addition agent such as sulphonated higher alcohols, etc. in either an acid or basic plating solution will form a low surface tension film on the surface of the bath and will effectively prevent the foam forming materials from interfering with the plating operation.
This invention is not limited only to nickel or copper plating but is also applicable to any acid plating solution such as cobalt, copper, nickel, lead, iron, zinc, etc. Chromium plating solutions, however, are an exception because their powerful oxidizing action destroys the organic alcohols.
Mildly alkaline plating solutions such as used for cadmium, copper, brass, silver, zinc, etc., may also be made non-foaming by adding a small percentage of the above described insoluble aliphatic alcohols to the solution containing non-pitting agents such as higher sulphonated alcohols and. the like.
The following are examples of non-foaming alkaline electrolytic plating baths in accordance with the invention.
Example 7 CuCN 22.5 g/l NaCN 34 g/l NazCO: 15 g/l Igepon T 3 g/l Octyl alcohol 4 g/l Suitable ranges for the contents of this bath are CuCN 15-60 grams per liter, NaCN 15-90 grams per liter, NazCOa 10-100 grams per liter,
Igepon T 1-20 grams per liter, octyl alcohol 2-10 grams per liter.
Suitable ranges for the contents of this bath are AgCN 15-45 grams per liter, KCN 17-20 grams per liter, K2003 15-70 grams per llter, Igepon T" 1-20 grams per liter, octyl alcohol 2-10 grams per liter.
It will be understood that in place of employing a single aliphatic alcohol in the above examples to prevent foaming of the electroplating bath, it is within the inventive concept to employ more than one of these alcohols in the same bath. However, in such event the total aliphatic alcohol content should be within the preferred range of approximately 0.2% to 10%.
By employing my invention I have been able to greatly facilitate and improve electroplating of articles in baths containing non-pitting or bright plating addition agents particularly when the article is rotated or removed frequently in the course of the plating operation.
What is claimed is:
1. The method of preventing foaming of electroplating baths containing addition agents which tend to produce foaming, which comprises adding to the bath a small amount of a saturated monohydric aliphatic alcohol having 5 to 10 carbon atoms said alcohol being insoluble in said plating bath.
2. The method of preventing foaming of electroplating baths containing addition agents which tend to produce foaming, which comprises adding to the bath a small amount of octyl alcohol, said alcohol being insoluble in said plating bath.
3. The method of preventing foaming of electroplating baths containing addition agents which when agitated during the plating operation tend to produce foaming, which comprises adding to the bath a small amount of a saturated monohydric aliphatic alcohol having a 5 to 10 carbon atom alkyl radicle, said alcohol being insoluble in said plating bath.
4. The method of preventing foaming of electroplating baths containing addition agents which when agitated during the plating operation tend to produce foaming, which comprises adding to the bath a small amount of octyl alcohol, said alcohol being insoluble in said plating bath.
5. The method of preventing foaming of electroplating baths containing higher sulphonated alcohol addition agents which comprises adding to the bath a small amount of a saturated monohydric aliphatic alcohol having 5 to 9 carbon atoms, said alcohol being insoluble in said plating bath.
6. The method of preventing foaming of electroplating baths containing higher sulphonated alcohol addition agents which comprises adding to the bath a small amount of octyl alcohol, said alcohol being insoluble in said plating bath.
7. The method of preventing foaming of electroplating baths containing higher sulphonated alcohol addition agents which comprises adding to the bath a small amount of a saturated monohydric aliphatic alcohol having 6 to 8 carbon atoms, said alcohol being insoluble in said platlng bath.
WIILIAM M. TUCKER.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US141972A US2147415A (en) | 1937-05-11 | 1937-05-11 | Electroplating |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US141972A US2147415A (en) | 1937-05-11 | 1937-05-11 | Electroplating |
Publications (1)
Publication Number | Publication Date |
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US2147415A true US2147415A (en) | 1939-02-14 |
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US141972A Expired - Lifetime US2147415A (en) | 1937-05-11 | 1937-05-11 | Electroplating |
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Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2495668A (en) * | 1946-12-21 | 1950-01-24 | Harshaw Chem Corp | Electrodeposition of copper |
US2519672A (en) * | 1947-01-13 | 1950-08-22 | Charles F Lawless | Composition for bluing metal |
US2519858A (en) * | 1944-09-29 | 1950-08-22 | Spiro Peter | Electrodeposition of nickel and nickel alloys |
US2525942A (en) * | 1945-06-29 | 1950-10-17 | Standard Oil Co | Electrodepositing bath and process |
US2575176A (en) * | 1947-12-15 | 1951-11-13 | Monsanto Chemicals | Water treating composition |
US2639997A (en) * | 1947-04-24 | 1953-05-26 | Int Standard Electric Corp | Metallization of nonmetallic surfaces |
US2684384A (en) * | 1943-07-15 | 1954-07-20 | Du Pont | Preparation of ethylenedinitramine |
US2827392A (en) * | 1955-08-31 | 1958-03-18 | Thomas Electronics Inc | Inhibition of bubble formation in a settling process |
US3472664A (en) * | 1966-09-15 | 1969-10-14 | Enthone | Inhibiting stardusting in electroless copper plating |
US4071468A (en) * | 1975-06-13 | 1978-01-31 | Ciba-Geigy Corporation | Wetting and anti-foaming agents, and process for removing foam from aqueous systems |
US4083936A (en) * | 1975-09-19 | 1978-04-11 | Woodward Fred E | Manufacture of phosphoric acid using acid phosphate ester antifoaming compositions |
US5066367A (en) * | 1981-09-11 | 1991-11-19 | Learonal Inc. | Limiting tin sludge formation in tin or tin/lead electroplating solutions |
US5094726A (en) * | 1981-09-11 | 1992-03-10 | Learonal, Inc. | Limiting tin sludge formation in tin or tin-lead electroplating solutions |
US5174887A (en) * | 1987-12-10 | 1992-12-29 | Learonal, Inc. | High speed electroplating of tinplate |
EP0786539A2 (en) | 1996-01-26 | 1997-07-30 | Elf Atochem North America, Inc. | High current density zinc organosulfonate electrogalvanizing process and composition |
-
1937
- 1937-05-11 US US141972A patent/US2147415A/en not_active Expired - Lifetime
Cited By (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2684384A (en) * | 1943-07-15 | 1954-07-20 | Du Pont | Preparation of ethylenedinitramine |
US2519858A (en) * | 1944-09-29 | 1950-08-22 | Spiro Peter | Electrodeposition of nickel and nickel alloys |
US2525942A (en) * | 1945-06-29 | 1950-10-17 | Standard Oil Co | Electrodepositing bath and process |
US2495668A (en) * | 1946-12-21 | 1950-01-24 | Harshaw Chem Corp | Electrodeposition of copper |
US2519672A (en) * | 1947-01-13 | 1950-08-22 | Charles F Lawless | Composition for bluing metal |
US2639997A (en) * | 1947-04-24 | 1953-05-26 | Int Standard Electric Corp | Metallization of nonmetallic surfaces |
US2575176A (en) * | 1947-12-15 | 1951-11-13 | Monsanto Chemicals | Water treating composition |
US2827392A (en) * | 1955-08-31 | 1958-03-18 | Thomas Electronics Inc | Inhibition of bubble formation in a settling process |
US3472664A (en) * | 1966-09-15 | 1969-10-14 | Enthone | Inhibiting stardusting in electroless copper plating |
US4071468A (en) * | 1975-06-13 | 1978-01-31 | Ciba-Geigy Corporation | Wetting and anti-foaming agents, and process for removing foam from aqueous systems |
US4092266A (en) * | 1975-06-13 | 1978-05-30 | Ciba-Geigy Corporation | Process for removing foam from aqueous systems and composition useful therein |
US4083936A (en) * | 1975-09-19 | 1978-04-11 | Woodward Fred E | Manufacture of phosphoric acid using acid phosphate ester antifoaming compositions |
US5066367A (en) * | 1981-09-11 | 1991-11-19 | Learonal Inc. | Limiting tin sludge formation in tin or tin/lead electroplating solutions |
US5094726A (en) * | 1981-09-11 | 1992-03-10 | Learonal, Inc. | Limiting tin sludge formation in tin or tin-lead electroplating solutions |
US5174887A (en) * | 1987-12-10 | 1992-12-29 | Learonal, Inc. | High speed electroplating of tinplate |
EP0786539A2 (en) | 1996-01-26 | 1997-07-30 | Elf Atochem North America, Inc. | High current density zinc organosulfonate electrogalvanizing process and composition |
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