US2442195A - Cleaning and electroplating process - Google Patents

Cleaning and electroplating process Download PDF

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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
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US
United States
Prior art keywords
metal
cleaning
copper
article
electroplating process
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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
Application number
US608089A
Inventor
James T Clenny
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
General Electric Co
Original Assignee
General Electric Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Priority to BE471083D priority Critical patent/BE471083A/xx
Application filed by General Electric Co filed Critical General Electric Co
Priority to US608089A priority patent/US2442195A/en
Priority to GB22077/46A priority patent/GB615110A/en
Priority to FR942946D priority patent/FR942946A/en
Application granted granted Critical
Publication of US2442195A publication Critical patent/US2442195A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25FPROCESSES FOR THE ELECTROLYTIC REMOVAL OF MATERIALS FROM OBJECTS; APPARATUS THEREFOR
    • C25F3/00Electrolytic etching or polishing
    • C25F3/16Polishing
    • C25F3/22Polishing of heavy metals
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D3/00Electroplating: Baths therefor
    • C25D3/66Electroplating: Baths therefor from melts
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D5/00Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
    • C25D5/18Electroplating using modulated, pulsed or reversing current
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D5/00Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
    • C25D5/34Pretreatment of metallic surfaces to be electroplated
    • C25D5/36Pretreatment of metallic surfaces to be electroplated of iron or steel
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D5/00Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
    • C25D5/627Electroplating characterised by the visual appearance of the layers, e.g. colour, brightness or mat appearance
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25FPROCESSES FOR THE ELECTROLYTIC REMOVAL OF MATERIALS FROM OBJECTS; APPARATUS THEREFOR
    • C25F1/00Electrolytic cleaning, degreasing, pickling or descaling
    • C25F1/02Pickling; Descaling
    • C25F1/12Pickling; Descaling in melts
    • C25F1/14Iron 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
US608089A 1945-07-31 1945-07-31 Cleaning and electroplating process Expired - Lifetime US2442195A (en)

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

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BE (1) BE471083A (en)
FR (1) FR942946A (en)
GB (1) GB615110A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2873233A (en) * 1956-03-21 1959-02-10 Philco Corp Method of electrodepositing metals

Citations (12)

* Cited by examiner, † Cited by third party
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

Patent Citations (12)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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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