US1916503A - Process of cleaning metal - Google Patents
Process of cleaning metal Download PDFInfo
- Publication number
- US1916503A US1916503A US475374A US47537430A US1916503A US 1916503 A US1916503 A US 1916503A US 475374 A US475374 A US 475374A US 47537430 A US47537430 A US 47537430A US 1916503 A US1916503 A US 1916503A
- Authority
- US
- United States
- Prior art keywords
- metal
- bath
- anode
- cleaning
- steel
- 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
- 229910052751 metal Inorganic materials 0.000 title description 38
- 239000002184 metal Substances 0.000 title description 38
- 238000004140 cleaning Methods 0.000 title description 19
- 238000000034 method Methods 0.000 title description 18
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 31
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 20
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 14
- 229910000831 Steel Inorganic materials 0.000 description 12
- 239000010959 steel Substances 0.000 description 12
- 229910052742 iron Inorganic materials 0.000 description 10
- 239000011248 coating agent Substances 0.000 description 9
- 238000000576 coating method Methods 0.000 description 9
- 239000000463 material Substances 0.000 description 9
- 239000000243 solution Substances 0.000 description 9
- 229910001369 Brass Inorganic materials 0.000 description 7
- 239000010951 brass Substances 0.000 description 7
- KRVSOGSZCMJSLX-UHFFFAOYSA-L chromic acid Substances O[Cr](O)(=O)=O KRVSOGSZCMJSLX-UHFFFAOYSA-L 0.000 description 7
- AWJWCTOOIBYHON-UHFFFAOYSA-N furo[3,4-b]pyrazine-5,7-dione Chemical compound C1=CN=C2C(=O)OC(=O)C2=N1 AWJWCTOOIBYHON-UHFFFAOYSA-N 0.000 description 7
- 229910052759 nickel Inorganic materials 0.000 description 7
- 229910000975 Carbon steel Inorganic materials 0.000 description 3
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 3
- 239000010962 carbon steel Substances 0.000 description 3
- 239000003792 electrolyte Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000005554 pickling Methods 0.000 description 3
- 239000001117 sulphuric acid Substances 0.000 description 3
- 235000011149 sulphuric acid Nutrition 0.000 description 3
- 239000003513 alkali Substances 0.000 description 2
- 239000004519 grease Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 241000357293 Leptobrama muelleri Species 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- WGLPBDUCMAPZCE-UHFFFAOYSA-N Trioxochromium Chemical compound O=[Cr](=O)=O WGLPBDUCMAPZCE-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 229910000423 chromium oxide Inorganic materials 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- -1 for example Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 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
- C25F1/06—Iron or steel
Definitions
- the sheet steel usually a commercial grade of carbon steel, is first cut and formed into the shape of half bearings, and is then washed in a hot alkali bath and rinsed in water. The piece is then cleaned in a hot alkali bath, electric current being passed through the bath,
- the iron tank serving as the anode serving as the anode, and the work as the cathode.
- the next step electric pickling in hydrochloric acid I have found it preferable to use a solution of 50% commercial hydrochloric acid sp. gr. 1.18).
- the bearing backs are suspended in the bath in lead holders.
- the tank is rubber lined.
- the bearings serve as the anodes.
- Lead cathodes are used. I prefer to use a current density of about 100 to 200 amperes per square foot and to continue the pickling for about five minutes.
- a chromic acid solution is used containing of approximately the following composition.
- the backs are then rinsed, immersed in a fiuxing bath, tinned and babbitted.
- Sulphuric acid may be used in place of the hydrochloric acid, although I havefoundthelatterpreferable. Itmaybedesirable to heat the hydrochloric or sulphuric acid bath, for in the use of the bath the iron from the bearings reduces the free acid and renders it less effective as time goes on and this would to some extent be counteracted by the use of heat. Fairly satisfactory results may be obtained by omitting the electrical treatment in the hydrochloric acid bath but this makes a longer period of treatment necessary.
- the method of cleaning carbon steel and analogous material which consists in immersing the metal in a bath of hydrochloric acid, to remove oxides and other foreign material from the surface of the metal and leaving a coating of oxidizable material thereon, and thereafter immersing the metal in a bath of chromic acid, and passing current through the bath with the metal acting as the anode to remove the oxidizable ma terial.
- the method of cleaning metal such as steel, iron, brass or nickel which consists in immersing the metal in a bath of hydrochloric acid, passing current through the bath with the metalacting as the anode to remove oxides and other foreign material from the surface of the metal and leaving a coating of oxidizable material thereon, and thereafter immersing the metal in a bath of chromic acid, and passing current through the bath with the metal acting as the anode to remove the oxidizable material.
- the method of cleaning carbon steel and analogous material which consists in immersing the material in a bath of hydrochloric acid, passing current through the bath with the metal acting as the anode to remove the oxide coating from the metal leaving a carbonaceous coating thereon, and thereafter immersing the metal in a chromic acid bath, and passing current through the bath with carbonaceous coating.
- the method of cleaning steel and the like which consists in subjectingthe object 'as an anode to the action'of an electric current having a density of approximately 100 to 200 amperes per square foot in a strong the metal acting as the anode, to remove the 4.
- the method of cleaning steel and the like which consists in subjecting the object as a cathode to the action of an alkaline electrolyte to remove grease and dirt, then subjecting the object as an anode to the action of hydrochloric acid to remove the oxide coating from the metal, said bath leaving an oxidizable coating on the metal, and thereafter subjecting the object'as an anode to the action of an electrolyte having as its principal active constituent chromic acid.
- the method of cleaning metal such as steel, iron, brass or nickel which comprises immersing the metal in a bath of hydrochloric acid and passing current through the bath with the metal acting as the anode.
- the method of cleaning metal such as steel, iron, brass or nickel which comprises immersing the metal in a bath of hydrochloric acid and passing current through the bath by means of lead cathodes, the metal to a be cleaned acting as the anode.
- the method of cleaning metal such as steel, iron, brass or nickel which comprises immersing the metal in a solution of approximately 50% hydrochloric acid and passing current through the bath with the metal acting as the anode.
- the method of cleaning metal such as steel, iron, brass or nickel which comprises immersing the metal in a solution of approximately 50% hydrochloric acid and passing current of the order of 100 to 200 amperes per square inch through the bath with themetal acting as the anode.
- the method of cleaning metal such as steel, iron, brass or nickel which consists in immersing the metal in an alkaline electrolyte and passing current through the bath with the metal acting as the cathode, and then immersing the object in a bath of hydrochloric acid and passing an electric current through the bath with the metal acting as the anode.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
- ing And Chemical Polishing (AREA)
Description
Patented July 4, 1933 UNITED STATES PATENT OFFICE AUSTIN B. WILSON, OF FLINT, MICHIGAN, ASSIGNOR TO GENERAL MOTORS CORPORA- TION, OF DETROIT, MICHIGAN, A CORPORATION OF DELAWARE PROCESS OF CLEANING METAL No Drawing.
In the manufacture of Babbitt lined steel; backed bearings it is customary to first shape the steel backs, then clean them, dip them in tin, and cast a lining of babbitt on the interior of the tinned back. It is essential that a good bond be formed between the back and the lining, otherwise the bearing will have short life. In order to get a good bond it is essential that the back be thoroughly cleaned so as to remove all oxide and other foreign material and it is also preferable that the back be slightly roughened. Ordinary methods used in cleaning metal have proven inadequate with the result that poor bonds are obtained.
The method of cleaning steel disclosed in this application fully satisfies the requirements above outlined and makes it possible to produce a bond which I believe is superior to any heretofore obtained. The method is not expensive and is being successfully used in production on a large scale.
The sheet steel, usually a commercial grade of carbon steel, is first cut and formed into the shape of half bearings, and is then washed in a hot alkali bath and rinsed in water. The piece is then cleaned in a hot alkali bath, electric current being passed through the bath,
the iron tank serving as the anode, and the work as the cathode. I have found it best to use a current density around 50 to 60 amperes per square foot and to continue the operation for about two minutes. In this and the other baths the voltage applied is not critical. I have used from 4 to 8 volts in accordance with current practice. The piece is then again rinsed.
' The above cleaning operations serve to remove the oil and grease from the surface 0 the piece.
The next step electric pickling in hydrochloric acid. I have found it preferable to use a solution of 50% commercial hydrochloric acid sp. gr. 1.18). The bearing backs are suspended in the bath in lead holders. The tank is rubber lined. The bearings serve as the anodes. Lead cathodes are used. I prefer to use a current density of about 100 to 200 amperes per square foot and to continue the pickling for about five minutes.
Application filed August 14, 1930. Serial 1T0. 475,374.
During this operation the oxide is removed to the next electric pickling operation. In
this operation a chromic acid solution is used containing of approximately the following composition.
CrO 200 grams per liter of solution H SO 2 grams per liter of solution This bath is preferably maintained at a temperature of about 100 to 130 degrees Fahrenheit by'means of a steam coil. The bearings are supported on lead holders and serve as the anode. The iron tank is the cathode. I have found it best to use a current density of from 50 to 150 amperes per square foot and to continue the operation for about one minute. We have found it necessary to vary the temperature or current density at times to remove stain from the metal.
1 As a result of this operation the carbonaceous deposit is removed from the surface of the metal, and I think the carbon is dissolved in the bath, for it is well known that chromic acid is a strong oxidizing agent. 7
As a result of the described cleaning operations, the backs now present an etched appearance, and while bright, look gray by comparison with their previous condition.
The backs are then rinsed, immersed in a fiuxing bath, tinned and babbitted.
The process described is capable of some modification. Sulphuric acid may be used in place of the hydrochloric acid, although I havefoundthelatterpreferable. Itmaybedesirable to heat the hydrochloric or sulphuric acid bath, for in the use of the bath the iron from the bearings reduces the free acid and renders it less effective as time goes on and this would to some extent be counteracted by the use of heat. Fairly satisfactory results may be obtained by omitting the electrical treatment in the hydrochloric acid bath but this makes a longer period of treatment necessary.
I have described my cleaning process used in the manufacture of bearings but it is obvious that it is of general utility for cleaning metals, for example, brass, nickel and iron. 5 ,I claim:
1. The method of cleaning carbon steel and analogous material which consists in immersing the metal in a bath of hydrochloric acid, to remove oxides and other foreign material from the surface of the metal and leaving a coating of oxidizable material thereon, and thereafter immersing the metal in a bath of chromic acid, and passing current through the bath with the metal acting as the anode to remove the oxidizable ma terial.
2. The method of cleaning metal such as steel, iron, brass or nickel which consists in immersing the metal in a bath of hydrochloric acid, passing current through the bath with the metalacting as the anode to remove oxides and other foreign material from the surface of the metal and leaving a coating of oxidizable material thereon, and thereafter immersing the metal in a bath of chromic acid, and passing current through the bath with the metal acting as the anode to remove the oxidizable material.
3. The method of cleaning carbon steel and analogous material, which consists in immersing the material in a bath of hydrochloric acid, passing current through the bath with the metal acting as the anode to remove the oxide coating from the metal leaving a carbonaceous coating thereon, and thereafter immersing the metal in a chromic acid bath, and passing current through the bath with carbonaceous coating.
like which consists in subjecting the object as an anode to the action of an electric current in a solution of approximately HCl to remove the oxide coating, said bath leaving an oxidizable deposit on the metal, and thereafter subjecting the object as an anode to the action of an electric current in an aqueous solution containing approximately 200 grams of chromium oxide and 2 grams of sulphuric acid per liter.
5. The method of cleaning steel and the like which consists in subjectingthe object 'as an anode to the action'of an electric current having a density of approximately 100 to 200 amperes per square foot in a strong the metal acting as the anode, to remove the 4. The method of cleaning steel and the' solution of hydrochloric acid to remove the oxide coating, said bath leaving an oxidizable deposit on the metal, and thereafter subjecting the object as an anode to the action of an electric current having a density of approximately 50 to 150 amperes per square foot, in a strong solution of chromic acid, to remove the deposit.
6,. The method of cleaning steel and the like which consists in subjecting the object as a cathode to the action of an alkaline electrolyte to remove grease and dirt, then subjecting the object as an anode to the action of hydrochloric acid to remove the oxide coating from the metal, said bath leaving an oxidizable coating on the metal, and thereafter subjecting the object'as an anode to the action of an electrolyte having as its principal active constituent chromic acid.
7. The method of cleaning metal such as steel, iron, brass or nickel which comprises immersing the metal in a bath of hydrochloric acid and passing current through the bath with the metal acting as the anode.
8. The method of cleaning metal such as steel, iron, brass or nickel which comprises immersing the metal in a bath of hydrochloric acid and passing current through the bath by means of lead cathodes, the metal to a be cleaned acting as the anode.
9. The method of cleaning metal such as steel, iron, brass or nickel which comprises immersing the metal in a solution of approximately 50% hydrochloric acid and passing current through the bath with the metal acting as the anode.
10. The method of cleaning metal such as steel, iron, brass or nickel which comprises immersing the metal in a solution of approximately 50% hydrochloric acid and passing current of the order of 100 to 200 amperes per square inch through the bath with themetal acting as the anode.
11. The method of cleaning metal such as steel, iron, brass or nickel which consists in immersing the metal in an alkaline electrolyte and passing current through the bath with the metal acting as the cathode, and then immersing the object in a bath of hydrochloric acid and passing an electric current through the bath with the metal acting as the anode.
In testimony whereof I afiix my signature.
AUSTIN B. WILSON.
III
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US475374A US1916503A (en) | 1930-08-14 | 1930-08-14 | Process of cleaning metal |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US475374A US1916503A (en) | 1930-08-14 | 1930-08-14 | Process of cleaning metal |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1916503A true US1916503A (en) | 1933-07-04 |
Family
ID=23887304
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US475374A Expired - Lifetime US1916503A (en) | 1930-08-14 | 1930-08-14 | Process of cleaning metal |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1916503A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2431947A (en) * | 1943-03-06 | 1947-12-02 | Gen Motors Corp | Formation of a strong bond between a ferrous metal surface and an electrodeposit of silver |
| US2730494A (en) * | 1950-09-16 | 1956-01-10 | Gen Motors Corp | Process of electrolytic deburring of metal |
| US3167493A (en) * | 1961-03-15 | 1965-01-26 | North American Aviation Inc | Manufacture of high-strength steel parts for use in aircraft and the like |
-
1930
- 1930-08-14 US US475374A patent/US1916503A/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2431947A (en) * | 1943-03-06 | 1947-12-02 | Gen Motors Corp | Formation of a strong bond between a ferrous metal surface and an electrodeposit of silver |
| US2730494A (en) * | 1950-09-16 | 1956-01-10 | Gen Motors Corp | Process of electrolytic deburring of metal |
| US3167493A (en) * | 1961-03-15 | 1965-01-26 | North American Aviation Inc | Manufacture of high-strength steel parts for use in aircraft and the like |
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