US1867527A - Process for anodic removal of surface metal film - Google Patents
Process for anodic removal of surface metal film Download PDFInfo
- Publication number
- US1867527A US1867527A US444613A US44461330A US1867527A US 1867527 A US1867527 A US 1867527A US 444613 A US444613 A US 444613A US 44461330 A US44461330 A US 44461330A US 1867527 A US1867527 A US 1867527A
- Authority
- US
- United States
- Prior art keywords
- film
- metal
- removal
- metal film
- anodic
- 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
- 239000002184 metal Substances 0.000 title description 23
- 229910052751 metal Inorganic materials 0.000 title description 23
- 238000000034 method Methods 0.000 title description 13
- 239000010408 film Substances 0.000 description 35
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 12
- 239000000243 solution Substances 0.000 description 11
- 229910019142 PO4 Inorganic materials 0.000 description 8
- 235000021317 phosphate Nutrition 0.000 description 8
- 229910000831 Steel Inorganic materials 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 6
- 229910052742 iron Inorganic materials 0.000 description 6
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 6
- 239000010452 phosphate Substances 0.000 description 6
- 239000010959 steel Substances 0.000 description 6
- 150000001450 anions Chemical class 0.000 description 5
- 239000003792 electrolyte Substances 0.000 description 5
- 239000002253 acid Substances 0.000 description 4
- 238000004090 dissolution Methods 0.000 description 4
- 150000002500 ions Chemical class 0.000 description 4
- 150000001642 boronic acid derivatives Chemical class 0.000 description 3
- 230000002633 protecting effect Effects 0.000 description 3
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 2
- 239000012670 alkaline solution Substances 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 2
- 150000004760 silicates Chemical class 0.000 description 2
- ATRRKUHOCOJYRX-UHFFFAOYSA-N Ammonium bicarbonate Chemical compound [NH4+].OC([O-])=O ATRRKUHOCOJYRX-UHFFFAOYSA-N 0.000 description 1
- DJHGAFSJWGLOIV-UHFFFAOYSA-K Arsenate3- Chemical class [O-][As]([O-])([O-])=O DJHGAFSJWGLOIV-UHFFFAOYSA-K 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000001099 ammonium carbonate Substances 0.000 description 1
- 235000012501 ammonium carbonate Nutrition 0.000 description 1
- KGBXLFKZBHKPEV-UHFFFAOYSA-N boric acid Chemical compound OB(O)O KGBXLFKZBHKPEV-UHFFFAOYSA-N 0.000 description 1
- 239000004327 boric acid Substances 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 238000005530 etching Methods 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- 238000010348 incorporation Methods 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- -1 phosphate Chemical class 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 230000036647 reaction Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 239000004332 silver Substances 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
Classifications
-
- 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
- C25F1/04—Pickling; Descaling in solution
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D11/00—Electrolytic coating by surface reaction, i.e. forming conversion layers
Definitions
- This invention relates to improvements in processes for defilming or for the removal of thin metallic films by anodic treatment in an aqueous electrolytic bath.
- My invention specifically pertains to the removal of such metal cess of hydrogen at the surface of the work and simultaneously depositing a continuouscoating of lead or other metal on the surface of the work, the metal coating or film preventing acid pitting and hydrogen embrittlement.
- the work with the metal film on its surface is made anode in an alkaline or acid bath.
- electrolyticcleaning processes have been suggested in the past, but, aside from my above-mentioned process, the only electrolytic cleaning method which is in use today is one in which the article is made cathode in an alkaline bath for the purpose of removing superficial grease or oil.
- One well known objection to this method is the serious embrittlement of the steel.
- my present process I use a solution in which the metal film is electrolytically soluble; as the metal of the film passes into solution, it interacts with the anions, such as phosphate, and thereby provides a new surface film which is both electrical current resisting and corrosion resisting. In this way the original film is completely removed without deleteriously affecting such as by etch the structure or quality of the underlying surface of the metal of the article.
- An important step in my invention embodies the incorporation in the electrolyte of salts or acids which will form comparatively insoluble products on the surface of the metallic article as fast as the metal film is removed therefrom.
- the thin film of phosphate produced 5 protects the underlying iron and steel from further anodlc action due partially to the high electrical resistance of these films diverting the current to such points or areas where the lead film has not yet been removed. If, in place of a lead or a zinc film, a tin film is to be removed, I prefer to substitute sodium carbonate for the sodium hydrate in the above bath. In place of an alkaline phosphate in the solution I can use borates, silicates, arsenates, antimonates.
- I may employ an acid solution such as sulfuric acidv solution containing phosphoric or boric acid
- the work is made anode and, as soon as the copper is removed and the bare iron or steel exposed underneath, a protective film of phosphate is formed as in the first illustration.
- ammoniacal solution can be used likewise for silver.
- nickel I prefer to add a small quantity of a soluble chloride to the ammoniacal solution.
- a process for the removal of metallic surface film which is characterized by the subjection of the'work to two simultaneous 0 reactions namely, the anodic dissolution of the metal composing the film and the simultaneous reaction of part of the ions of the metal film with such anions of the electrolyte as to produce a new insoluble film protecting 15 the metal of the work from etching or 001'- rosion.
- a process for the removing of lead surface films from iron and steel castings which is characterized by the subjection of the work 59 to two simultaneous anodic electrolytic actions in an alkaline phosphate bath whereby the lead film is dissolved and simultaneous therewith lead'ions formed by the dissolution q of film react to produce upon the denuded article an electric current and corrosion resisting film.
- a process for the removal of metallic surface film which is characterized by the subjection of the work to two simultaneous reactions in an alkaline electrolyte, namely, the anodic dissolution of the metal composing the film and the simultaneous reaction of part of the ions of the metal film with such anions of the electrolyte as to produce a new, insollcuble film protecting the metal of the wor 4.
- a process for the removal of metallic surface film which is characterized by the sub- 0 jection of the work to two simultaneous reac tions in an alkaline solution containing anions of the group including phosphates, borates, and silicates, namely: the anodic dissolution of the metal composing the fihn and the simultaneous reaction of part of the ions of the metal film with such anions of the electrolyte as to produce a new insoluble film pro tecting the metal of the work.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- ing And Chemical Polishing (AREA)
- Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
Description
Patented July 12, 1932 {UNITED STATES PATENT orrlce THOMAS E. DUNN, OF BRIDGEPORT, CONNECTICUT, ASSIGNOR TO THE BULLABD COM- PANY, OF BRIDGEPORT, CONNECTICUT, A CORPORATION OF CONNECTICUT PROCESS FOR ANODIC REMOVAL OF SURFACE METAL FILM F0 Drawing.
This invention relates to improvements in processes for defilming or for the removal of thin metallic films by anodic treatment in an aqueous electrolytic bath. My invention specifically pertains to the removal of such metal cess of hydrogen at the surface of the work and simultaneously depositing a continuouscoating of lead or other metal on the surface of the work, the metal coating or film preventing acid pitting and hydrogen embrittlement.
According to my present invention the work with the metal film on its surface is made anode in an alkaline or acid bath. I am aware that electrolyticcleaning processes have been suggested in the past, but, aside from my above-mentioned process, the only electrolytic cleaning method which is in use today is one in which the article is made cathode in an alkaline bath for the purpose of removing superficial grease or oil. One well known objection to this method is the serious embrittlement of the steel. In my present process I use a solution in which the metal film is electrolytically soluble; as the metal of the film passes into solution, it interacts with the anions, such as phosphate, and thereby provides a new surface film which is both electrical current resisting and corrosion resisting. In this way the original film is completely removed without deleteriously affecting such as by etch the structure or quality of the underlying surface of the metal of the article. I
An important step in my invention embodies the incorporation in the electrolyte of salts or acids which will form comparatively insoluble products on the surface of the metallic article as fast as the metal film is removed therefrom.
now describe the application to the removal of lead films from iron. and steel articles. For this purpose I employ an alkaline solution Application filed April 15, 1980. Serial N0. 444,618.
which iron when serving as anode is almost insoluble. To further increase the insolub1l1ty of the II'OIl, I incorporate in the solution small quantities of phosphates, borates,
tures. The thin film of phosphate produced 5 protects the underlying iron and steel from further anodlc action due partially to the high electrical resistance of these films diverting the current to such points or areas where the lead film has not yet been removed. If, in place of a lead or a zinc film, a tin film is to be removed, I prefer to substitute sodium carbonate for the sodium hydrate in the above bath. In place of an alkaline phosphate in the solution I can use borates, silicates, arsenates, antimonates.
As a second illustration I cite the removal of copper films from iron or steel surfaces.
Although I may employ an acid solution such as sulfuric acidv solution containing phosphoric or boric acid, I prefer to employ an ammoniacal solution containing a soluble phosphate and ammonium carbonate. Here, again, the work is made anode and, as soon as the copper is removed and the bare iron or steel exposed underneath, a protective film of phosphate is formed as in the first illustration.
The above ammoniacal solution can be used likewise for silver. In the case of nickel I prefer to add a small quantity of a soluble chloride to the ammoniacal solution.
compounds, in'which the metalor metals of the article proper will be insoluble. As an illustration of my invention I shall In .my process the tworeactions are of a purely anodic, electrolytic character, the metal of the film passing into solution, and the exposed metal underneath the film being si- In general, then, I select my solution in such a way that the metal of the'film will form multaneously protected by a dense, though thin, film having a relativel high electrical resistance, besides the valua le corrosion-rev sistant property.
5 Having thus described my invention I claim: a
1. A process for the removal of metallic surface film which is characterized by the subjection of the'work to two simultaneous 0 reactions namely, the anodic dissolution of the metal composing the film and the simultaneous reaction of part of the ions of the metal film with such anions of the electrolyte as to produce a new insoluble film protecting 15 the metal of the work from etching or 001'- rosion.
2. A process for the removing of lead surface films from iron and steel castings which is characterized by the subjection of the work 59 to two simultaneous anodic electrolytic actions in an alkaline phosphate bath whereby the lead film is dissolved and simultaneous therewith lead'ions formed by the dissolution q of film react to produce upon the denuded article an electric current and corrosion resisting film. 1
- 3. A process for the removal of metallic surface film which is characterized by the subjection of the work to two simultaneous reactions in an alkaline electrolyte, namely, the anodic dissolution of the metal composing the film and the simultaneous reaction of part of the ions of the metal film with such anions of the electrolyte as to produce a new, insollcuble film protecting the metal of the wor 4. A process for the removal of metallic surface film which is characterized by the sub- 0 jection of the work to two simultaneous reac tions in an alkaline solution containing anions of the group including phosphates, borates, and silicates, namely: the anodic dissolution of the metal composing the fihn and the simultaneous reaction of part of the ions of the metal film with such anions of the electrolyte as to produce a new insoluble film pro tecting the metal of the work.
Signed at Bridgeport in the county of so Fairfield and State of Connecticut this 9th day of April, A. D. 1930.
THOMAS E. DUNN.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US444613A US1867527A (en) | 1930-04-15 | 1930-04-15 | Process for anodic removal of surface metal film |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US444613A US1867527A (en) | 1930-04-15 | 1930-04-15 | Process for anodic removal of surface metal film |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1867527A true US1867527A (en) | 1932-07-12 |
Family
ID=23765621
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US444613A Expired - Lifetime US1867527A (en) | 1930-04-15 | 1930-04-15 | Process for anodic removal of surface metal film |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1867527A (en) |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2428141A (en) * | 1940-09-25 | 1947-09-30 | Gen Motors Corp | Process for cleaning, stripping, and polishing metal surfaces |
| US2541275A (en) * | 1943-11-09 | 1951-02-13 | Alais & Froges & Camarque Cie | Apparatus for the electrolytic oxidation of metallic elements |
| US2578898A (en) * | 1948-08-20 | 1951-12-18 | Rca Corp | Electrolytic removal of metallic coatings from various base metals |
| US2590927A (en) * | 1948-07-17 | 1952-04-01 | Westinghouse Electric Corp | Electrolytic method of removing burrs |
| US2796394A (en) * | 1954-11-22 | 1957-06-18 | Clevitc Corp | Separating and recovering nonferrous alloys from ferrous materials coated therewith |
| US2907700A (en) * | 1948-03-25 | 1959-10-06 | Kolodney Morris | Stripping process for plutonium |
| US3178305A (en) * | 1962-05-04 | 1965-04-13 | United States Steel Corp | Method of making galvanized sheet steel coated on one side |
| US3231503A (en) * | 1964-01-30 | 1966-01-25 | Macdermid Inc | Ammoniacal aqueous solution containing sodium chlorite and used for dissolving metals |
| US3544390A (en) * | 1967-12-04 | 1970-12-01 | Siderurgie Fse Inst Rech | Phosphatizing process for iron products and products obtained thereby |
| US5384026A (en) * | 1993-09-24 | 1995-01-24 | Gold Effects, Inc. | Method for gold plating a metallic surface |
-
1930
- 1930-04-15 US US444613A patent/US1867527A/en not_active Expired - Lifetime
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2428141A (en) * | 1940-09-25 | 1947-09-30 | Gen Motors Corp | Process for cleaning, stripping, and polishing metal surfaces |
| US2541275A (en) * | 1943-11-09 | 1951-02-13 | Alais & Froges & Camarque Cie | Apparatus for the electrolytic oxidation of metallic elements |
| US2907700A (en) * | 1948-03-25 | 1959-10-06 | Kolodney Morris | Stripping process for plutonium |
| US2590927A (en) * | 1948-07-17 | 1952-04-01 | Westinghouse Electric Corp | Electrolytic method of removing burrs |
| US2578898A (en) * | 1948-08-20 | 1951-12-18 | Rca Corp | Electrolytic removal of metallic coatings from various base metals |
| US2796394A (en) * | 1954-11-22 | 1957-06-18 | Clevitc Corp | Separating and recovering nonferrous alloys from ferrous materials coated therewith |
| US3178305A (en) * | 1962-05-04 | 1965-04-13 | United States Steel Corp | Method of making galvanized sheet steel coated on one side |
| US3231503A (en) * | 1964-01-30 | 1966-01-25 | Macdermid Inc | Ammoniacal aqueous solution containing sodium chlorite and used for dissolving metals |
| US3544390A (en) * | 1967-12-04 | 1970-12-01 | Siderurgie Fse Inst Rech | Phosphatizing process for iron products and products obtained thereby |
| US5384026A (en) * | 1993-09-24 | 1995-01-24 | Gold Effects, Inc. | Method for gold plating a metallic surface |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US3654099A (en) | Cathodic activation of stainless steel | |
| US2132439A (en) | Method of producing phosphate coated ferrous articles | |
| US1867527A (en) | Process for anodic removal of surface metal film | |
| US3649491A (en) | Electrolytic stripping composition | |
| US1954473A (en) | Electrochemical process for removing scale and oxide from the surface of stainless steel | |
| US2067007A (en) | Method of coating metal | |
| US2949411A (en) | Titanium anodizing process | |
| US6332970B1 (en) | Electrolytic method of and compositions for stripping electroless nickel | |
| US3257299A (en) | Composition and method for electrolytic stripping of coatings from metals | |
| US2748066A (en) | Process of enameling steel | |
| US2423624A (en) | Indium plating | |
| US2578898A (en) | Electrolytic removal of metallic coatings from various base metals | |
| US2287948A (en) | Indium plating | |
| JP2011102411A (en) | Stainless steel product having conductivity, and method for manufacturing the same | |
| US2504272A (en) | Electrodeposition of silver | |
| US2581490A (en) | Electrolytic process of stripping metallic coatings from a ferrous metal base | |
| US2549411A (en) | Electrolytic stripping of nickel coatings from ferrous metals | |
| US2516227A (en) | Electroplating of chromiummolybdenum alloys | |
| JPS582593B2 (en) | Method for obtaining lead by electrolysis and electrolyte solution therefor | |
| US2553449A (en) | Process for obtaining by galvanic means a coating for protecting magnesium from corrosion | |
| US2436244A (en) | Metalworking and strippingplating process | |
| US2095519A (en) | Method for producing galvanic coatings on aluminum or aluminum alloys | |
| US2322205A (en) | Method of treating magnesium and its alloys | |
| US2118956A (en) | Method of chromium plating | |
| US2154469A (en) | Bright dip |