US2442195A - Cleaning and electroplating process - Google Patents
Cleaning and electroplating process Download PDFInfo
- Publication number
- US2442195A US2442195A US608089A US60808945A US2442195A US 2442195 A US2442195 A US 2442195A US 608089 A US608089 A US 608089A US 60808945 A US60808945 A US 60808945A US 2442195 A US2442195 A US 2442195A
- Authority
- US
- United States
- Prior art keywords
- metal
- cleaning
- copper
- article
- electroplating process
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25F—PROCESSES FOR THE ELECTROLYTIC REMOVAL OF MATERIALS FROM OBJECTS; APPARATUS THEREFOR
- C25F3/00—Electrolytic etching or polishing
- C25F3/16—Polishing
- C25F3/22—Polishing of heavy metals
-
- 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
- C25D3/66—Electroplating: Baths therefor from melts
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D5/00—Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
- C25D5/18—Electroplating using modulated, pulsed or reversing current
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D5/00—Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
- C25D5/34—Pretreatment of metallic surfaces to be electroplated
- C25D5/36—Pretreatment of metallic surfaces to be electroplated of iron or steel
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D5/00—Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
- C25D5/627—Electroplating characterised by the visual appearance of the layers, e.g. colour, brightness or mat appearance
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25F—PROCESSES FOR THE ELECTROLYTIC REMOVAL OF MATERIALS FROM OBJECTS; APPARATUS THEREFOR
- C25F1/00—Electrolytic cleaning, degreasing, pickling or descaling
- C25F1/02—Pickling; Descaling
- C25F1/12—Pickling; Descaling in melts
- C25F1/14—Iron or steel
Definitions
- the present invention relates to the surface treatment of metal articles with the object of removing adherent surface contaminations, including inorganic material such as rust and scale, and also organic material such as grease and oil.
- the cleaned surface by a step in the same process, is prepared by the electrolytic deposition of a metal which will facilitate the subsequent application by casting or otherwise of an unlike metal and thereby cause it to make a firm union with the cleaned and coated surface.
- My invention is applicable in particular to cleaning of metal castings, rolled plate, or forgings, and the subsequent application thereto of an unlike metal, for example Babbitt metal, to proludecomposite articles.
- My invention is particularly applicable to the manufacture of bearings.
- the cleaned metal surface next should be coated with a nonferrous metal which both protects the cleaned surface of the ferrous metal from reoxidation and prompts alloyage with a non-ferrous metal.
- a fused alkali electrolyte which may consist of a strong alkali, preferably caustic soda, having dissolved therein a suitable copper compound which is especially adaptable to the manufacture or bearings, for example one to ten per cent of copper oxide (CuO).
- a suitable copper compound which is especially adaptable to the manufacture or bearings, for example one to ten per cent of copper oxide (CuO).
- CuO copper oxide
- oxides and metallic salts of other oxidation-resisting non-ferrous metals ' may be used.
- metals of the group 1 Claim. (Cl. 204-34) consisting of copper, nickel and silver can be used in a similar manner for various applications as protective coatings on metal surfaces.
- the castings are immersed in such alkali bath which may be heated to a temperature in the range of 400 to 500 C.
- the articles to be treated are connected to an electric circuit charged with direct current at a potential of about three to six volts, the polarity of the castings first bein made positive.
- the negative cooperating electrode may be constituted by the container for the electrolyte or by a suitably spaced electrode which is connected to the negative terminal of the circuit.
- Theresulting passage ofcurrent causes oxidation and removal of the grease and'other organic matter from the surface of themetal article.
- the anodic treatment is continued for only a short time. About one minute is satis-- factory, the length of time not being critical.
- the current value may be about to 200 amperes per square foot of surface.
- the polarity thereupon being cleaned becoming the cathode.
- the cathodic treatment is continued at approximately the same current density until adherent scale and rust are removed. In general, about seven minutes is satisfactory.
- the third step is carried out by reducing the voltage, and thereby the current, to approximately one-tenth of the original density and by charging the casting again to positive potential, that is, reversing the polarity.
- the spongy, loosely adherent copper which was deposited as an unavoidable incident during the previous step is caused to g0 into solution.
- the metal article is charged negatively, that is, becomes cathodic for the electrolytic action occurring in the fused bath.
- the fourth step which is continued for about ten minutes, copper is deposited as a homogeneous, adherent layer on the ferrous metal object by electrolytic action, the current still being maintained at about 25 amperes per square foot.
- the ferrous metal object upon the completion of the copper coating step, is removed from the fused bath and immersed in water.
- the water dissolves the adherent coating of electrolyte.
- the surface of the ferrous metal article upon removal from the fused bath is copper-colored and retains this color after its immersion in water. The indications are that the copper coating becomes alloyed with the surface of the ferrous metal article.
- coated metal article is coated with a suitable is reversed, the article flux, for example, a flux containing zinc and ammonium chlorides.
- the followin flux is il-
- the article is then coated with tin, eitherby being preferably immersed in a bath of molten tin or having the molten tin way.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Coating With Molten Metal (AREA)
- Electroplating Methods And Accessories (AREA)
Description
Patented May 25, 1948 2,442,195 CLEANING AND ELECTROPLATING PROCESS James T. Clenny, Swampscott, General Electric Company,
New York Mass., assignor to a corporation of Nollrawing. Application July 31, 1945, Serial No. 608,089
The present invention relates to the surface treatment of metal articles with the object of removing adherent surface contaminations, including inorganic material such as rust and scale, and also organic material such as grease and oil. The cleaned surface, by a step in the same process, is prepared by the electrolytic deposition of a metal which will facilitate the subsequent application by casting or otherwise of an unlike metal and thereby cause it to make a firm union with the cleaned and coated surface.
'My invention is applicable in particular to cleaning of metal castings, rolled plate, or forgings, and the subsequent application thereto of an unlike metal, for example Babbitt metal, to pro ducecomposite articles. My invention is particularly applicable to the manufacture of bearings.
'I-Ieretofore metal objects which were coated with oil or grease, and also with rust or other oxides. have been subjected to a succession of independent stripping operations in order to remove such undesired surface contaminations. The cleaning operations in some cases were followered by an electrolytic treatment for depositing a coating metal. Commonly the cleaning operations included pickling in an aqueous solution of a strong acid which is not desirable and is not suitable for carrying out a plating operation.
In accordance with my invention I have provided a procedure comprising the combination of a plurality of electrolytic steps carried out successively in a single fused electrolyte in which the metal object to be cleaned functions alter nately as anode and cathode, As a consequence, the treatment of the metal is simplified, short ened in time and made more efficient.
For example, in the course of manufacture of ferrous bearings for rotating machinery, it is required to remove adherent rust, scale and grease, and it is desirable also that the cleaned metal surface next should be coated with a nonferrous metal which both protects the cleaned surface of the ferrous metal from reoxidation and prompts alloyage with a non-ferrous metal.
These objects of my invention are attained by a combination of chemical and electrochemical operations carried out in sequence in a fused alkali electrolyte which may consist of a strong alkali, preferably caustic soda, having dissolved therein a suitable copper compound which is especially adaptable to the manufacture or bearings, for example one to ten per cent of copper oxide (CuO). However, oxides and metallic salts of other oxidation-resisting non-ferrous metals 'may be used. In general, metals of the group 1 Claim. (Cl. 204-34) consisting of copper, nickel and silver can be used in a similar manner for various applications as protective coatings on metal surfaces.
The castings are immersed in such alkali bath which may be heated to a temperature in the range of 400 to 500 C. The articles to be treated are connected to an electric circuit charged with direct current at a potential of about three to six volts, the polarity of the castings first bein made positive. The negative cooperating electrode may be constituted by the container for the electrolyte or by a suitably spaced electrode which is connected to the negative terminal of the circuit. Theresulting passage ofcurrent causes oxidation and removal of the grease and'other organic matter from the surface of themetal article. The anodic treatment is continued for only a short time. About one minute is satis-- factory, the length of time not being critical. The current value may be about to 200 amperes per square foot of surface.
The polarity thereupon being cleaned becoming the cathode. The cathodic treatment is continued at approximately the same current density until adherent scale and rust are removed. In general, about seven minutes is satisfactory.
The third step is carried out by reducing the voltage, and thereby the current, to approximately one-tenth of the original density and by charging the casting again to positive potential, that is, reversing the polarity. By this step the spongy, loosely adherent copper which was deposited as an unavoidable incident during the previous step is caused to g0 into solution.
Finally, the metal article is charged negatively, that is, becomes cathodic for the electrolytic action occurring in the fused bath. During the fourth step, which is continued for about ten minutes, copper is deposited as a homogeneous, adherent layer on the ferrous metal object by electrolytic action, the current still being maintained at about 25 amperes per square foot.
The ferrous metal object, upon the completion of the copper coating step, is removed from the fused bath and immersed in water. The water dissolves the adherent coating of electrolyte. The surface of the ferrous metal article upon removal from the fused bath is copper-colored and retains this color after its immersion in water. The indications are that the copper coating becomes alloyed with the surface of the ferrous metal article.
the surface of the copper- As the final step, coated metal article is coated with a suitable is reversed, the article flux, for example, a flux containing zinc and ammonium chlorides. The followin flux is il- Upon removal from the flux bath, the article is then coated with tin, eitherby being preferably immersed in a bath of molten tin or having the molten tin way.
applied in any otherconvenient tin; or 4 copper,
or no-s'egreg'ating of alloying constituents.
What- I claim as new and desire to secure by Letters Patent 01" the United States is:
The process of cleaning and copperplating the current through said bath the articleto the following series of electrolytic and article to subject of alloys of copper, antimony and tin in the fol-5' JAMES T. CLENNY.
REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS Number Name Date. 1,004,673 Monnot Oct. 3, 191-1 1,417,896 Fletcher May 30, 1922 1,600,355 Otis et al Sept. 21,1926 1,795,512 Schmidt eta! Mar 10; 193 1 1,909,149 Hitner- May 16; 1933- 2,042,800- Pike June 2, 1936 2,134,457 Tainton Oct, 25;,1938 2,311,139 Tainton Feb.,16-,19,43; 2,327,676 Spence '24, 19.413 2,366,477 Bayley Jan..v2,- 1.945 2,395,694 Spence et al Feb. '26; 1946 FOREIGN PATENTS Number Country Date.
Great Britain, V Mar. 13,1935
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
BE471083D BE471083A (en) | 1945-07-31 | ||
US608089A US2442195A (en) | 1945-07-31 | 1945-07-31 | Cleaning and electroplating process |
GB22077/46A GB615110A (en) | 1945-07-31 | 1946-07-24 | Improvements in and relating to cleaning and electro-plating processes |
FR942946D FR942946A (en) | 1945-07-31 | 1947-02-04 | Electrolytic polishing |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US608089A US2442195A (en) | 1945-07-31 | 1945-07-31 | Cleaning and electroplating process |
Publications (1)
Publication Number | Publication Date |
---|---|
US2442195A true US2442195A (en) | 1948-05-25 |
Family
ID=24434982
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US608089A Expired - Lifetime US2442195A (en) | 1945-07-31 | 1945-07-31 | Cleaning and electroplating process |
Country Status (4)
Country | Link |
---|---|
US (1) | US2442195A (en) |
BE (1) | BE471083A (en) |
FR (1) | FR942946A (en) |
GB (1) | GB615110A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2547510A (en) * | 1949-01-08 | 1951-04-03 | J H Shoemaker | Composition and process for electrolytic cleaning of metals |
US3048497A (en) * | 1958-02-18 | 1962-08-07 | Moller Goran August | Process of coating base metals with aluminum |
US3053702A (en) * | 1959-05-19 | 1962-09-11 | Gennsalt Chemicals Corp | Metal coating |
US3507757A (en) * | 1966-04-04 | 1970-04-21 | Jacques Jean Caubet | Treatment of metal surfaces |
FR2502647A1 (en) * | 1981-03-27 | 1982-10-01 | Inst Metiznoi Promy | Prodn. of elongated brass-plated articles, e.g. wire - by subjecting a blank to a series of treatments including degreasing and etching, and also thermo-diffusing and tempering in salt bath |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2873233A (en) * | 1956-03-21 | 1959-02-10 | Philco Corp | Method of electrodepositing metals |
Citations (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1004673A (en) * | 1908-12-23 | 1911-10-03 | Duplex Metals Company | Process of and apparatus for making clad metals. |
US1417896A (en) * | 1920-01-28 | 1922-05-30 | Fletcher Electro Salvage Compa | Electrodeposition of metals upon iron and alloys of iron |
US1600355A (en) * | 1925-03-19 | 1926-09-21 | Nat Boiler Washing Company | Coating metal pipe with metal |
US1795512A (en) * | 1926-04-01 | 1931-03-10 | Metal & Thermit Corp | Process for the production of electrolytic deposits |
US1909149A (en) * | 1930-06-16 | 1933-05-16 | Pittsburgh Plate Glass Co | Method of preparing articles for plating |
GB425385A (en) * | 1933-12-15 | 1935-03-13 | William Edward Ballard | An improved method of manufacturing bearings of composite metals |
US2042800A (en) * | 1929-03-09 | 1936-06-02 | Kalif Corp | Process and apparatus for making bearings |
US2134457A (en) * | 1937-03-02 | 1938-10-25 | Tainton Urlyn Clifton | Metal treatment |
US2311139A (en) * | 1938-10-21 | 1943-02-16 | Tainton Urlyn Clifton | Process for the electrolytic cleaning of metals |
US2327676A (en) * | 1940-01-09 | 1943-08-24 | Repel Corp Du | Plating process |
US2366477A (en) * | 1939-06-22 | 1945-01-02 | William Bayley Company | Protective coating |
US2395694A (en) * | 1944-06-02 | 1946-02-26 | Hooker Electrochemical Co | Processes for removing oxide from the surface of metals |
-
0
- BE BE471083D patent/BE471083A/xx unknown
-
1945
- 1945-07-31 US US608089A patent/US2442195A/en not_active Expired - Lifetime
-
1946
- 1946-07-24 GB GB22077/46A patent/GB615110A/en not_active Expired
-
1947
- 1947-02-04 FR FR942946D patent/FR942946A/en not_active Expired
Patent Citations (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1004673A (en) * | 1908-12-23 | 1911-10-03 | Duplex Metals Company | Process of and apparatus for making clad metals. |
US1417896A (en) * | 1920-01-28 | 1922-05-30 | Fletcher Electro Salvage Compa | Electrodeposition of metals upon iron and alloys of iron |
US1600355A (en) * | 1925-03-19 | 1926-09-21 | Nat Boiler Washing Company | Coating metal pipe with metal |
US1795512A (en) * | 1926-04-01 | 1931-03-10 | Metal & Thermit Corp | Process for the production of electrolytic deposits |
US2042800A (en) * | 1929-03-09 | 1936-06-02 | Kalif Corp | Process and apparatus for making bearings |
US1909149A (en) * | 1930-06-16 | 1933-05-16 | Pittsburgh Plate Glass Co | Method of preparing articles for plating |
GB425385A (en) * | 1933-12-15 | 1935-03-13 | William Edward Ballard | An improved method of manufacturing bearings of composite metals |
US2134457A (en) * | 1937-03-02 | 1938-10-25 | Tainton Urlyn Clifton | Metal treatment |
US2311139A (en) * | 1938-10-21 | 1943-02-16 | Tainton Urlyn Clifton | Process for the electrolytic cleaning of metals |
US2366477A (en) * | 1939-06-22 | 1945-01-02 | William Bayley Company | Protective coating |
US2327676A (en) * | 1940-01-09 | 1943-08-24 | Repel Corp Du | Plating process |
US2395694A (en) * | 1944-06-02 | 1946-02-26 | Hooker Electrochemical Co | Processes for removing oxide from the surface of metals |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2547510A (en) * | 1949-01-08 | 1951-04-03 | J H Shoemaker | Composition and process for electrolytic cleaning of metals |
US3048497A (en) * | 1958-02-18 | 1962-08-07 | Moller Goran August | Process of coating base metals with aluminum |
US3053702A (en) * | 1959-05-19 | 1962-09-11 | Gennsalt Chemicals Corp | Metal coating |
US3507757A (en) * | 1966-04-04 | 1970-04-21 | Jacques Jean Caubet | Treatment of metal surfaces |
FR2502647A1 (en) * | 1981-03-27 | 1982-10-01 | Inst Metiznoi Promy | Prodn. of elongated brass-plated articles, e.g. wire - by subjecting a blank to a series of treatments including degreasing and etching, and also thermo-diffusing and tempering in salt bath |
Also Published As
Publication number | Publication date |
---|---|
FR942946A (en) | 1949-02-22 |
GB615110A (en) | 1948-01-03 |
BE471083A (en) |
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