US1729607A - Process for electrodeposition of metal - Google Patents
Process for electrodeposition of metal Download PDFInfo
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- US1729607A US1729607A US484785A US48478521A US1729607A US 1729607 A US1729607 A US 1729607A US 484785 A US484785 A US 484785A US 48478521 A US48478521 A US 48478521A US 1729607 A US1729607 A US 1729607A
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- US
- United States
- Prior art keywords
- electrolyte
- iron
- article
- metal
- coated
- 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 31
- 239000002184 metal Substances 0.000 title description 31
- 238000000034 method Methods 0.000 title description 20
- 238000004070 electrodeposition Methods 0.000 title description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical group [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 44
- 239000003792 electrolyte Substances 0.000 description 40
- 229910052742 iron Inorganic materials 0.000 description 16
- 239000000243 solution Substances 0.000 description 16
- 238000000151 deposition Methods 0.000 description 14
- 238000000576 coating method Methods 0.000 description 13
- 150000002739 metals Chemical group 0.000 description 12
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 11
- 239000001257 hydrogen Substances 0.000 description 10
- 229910052739 hydrogen Inorganic materials 0.000 description 10
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 9
- 239000011248 coating agent Substances 0.000 description 8
- 230000008021 deposition Effects 0.000 description 7
- 239000007789 gas Substances 0.000 description 7
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 6
- 239000000725 suspension Substances 0.000 description 6
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 description 5
- NCNCGGDMXMBVIA-UHFFFAOYSA-L iron(ii) hydroxide Chemical compound [OH-].[OH-].[Fe+2] NCNCGGDMXMBVIA-UHFFFAOYSA-L 0.000 description 5
- 239000002253 acid Substances 0.000 description 4
- 230000001464 adherent effect Effects 0.000 description 4
- 229910052782 aluminium Inorganic materials 0.000 description 4
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 4
- 239000011790 ferrous sulphate Substances 0.000 description 4
- 235000003891 ferrous sulphate Nutrition 0.000 description 4
- 235000014413 iron hydroxide Nutrition 0.000 description 4
- 229910000359 iron(II) sulfate Inorganic materials 0.000 description 4
- 229910000838 Al alloy Inorganic materials 0.000 description 3
- 229910045601 alloy Inorganic materials 0.000 description 3
- 239000000956 alloy Substances 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 238000009713 electroplating Methods 0.000 description 2
- 238000005530 etching Methods 0.000 description 2
- 229910017604 nitric acid Inorganic materials 0.000 description 2
- 230000002035 prolonged effect Effects 0.000 description 2
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- 239000000908 ammonium hydroxide Substances 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 229960002089 ferrous chloride Drugs 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- VKYKSIONXSXAKP-UHFFFAOYSA-N hexamethylenetetramine Chemical compound C1N(C2)CN3CN1CN2C3 VKYKSIONXSXAKP-UHFFFAOYSA-N 0.000 description 1
- 150000002506 iron compounds Chemical class 0.000 description 1
- NMCUIPGRVMDVDB-UHFFFAOYSA-L iron dichloride Chemical compound Cl[Fe]Cl NMCUIPGRVMDVDB-UHFFFAOYSA-L 0.000 description 1
- 159000000014 iron salts Chemical class 0.000 description 1
- 229910021506 iron(II) hydroxide Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000012047 saturated solution Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
Classifications
-
- 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
- C25D3/20—Electroplating: Baths therefor from solutions of iron
Definitions
- This invention relates generally to the electrolytic deposition of metals and more particularly to a process for depositing metals of the iron group on articles composed of 5 aluminum and its alloys.
- One object of the invention is to provide a process by which firmly adherent and smooth coatings of metals of the iron group mayAbe cheaply and easily deposited upon electrically conductive surfacest
- Another object is to provide a process of depositing smooth, soft coatings of iron on articles composed of aluminum and its alloys.
- Another object is to provide a new and iml5 proved electrolyte which, in addition to performing the usual functions of an ordinary electrolyte, is capable of maintaining substantially constant its initial degree of acidity or hydrogen concentration and when suitably l0 agitated, of effectively preventing adherence of gases to the surface to be coated.
- the electric current liberates free acid when it deposits metal from the electrolyte and then immediately causes combination of the free acid with a corresponding amount of metal from a metal electrode thereby maintaining constant the original acidity or hydrogen concentration of the electrolyte.
- an excess of free acid tends to accumulate as the process of deposition proceeds and the increased acidity or hydrogen concentration of the electrolyte is visibly indicated by the collection on the article being coated of bubbles of gas which is mainly hydrogen.
- hydrogen also causes brittleness and peeling of the deposited metal by reason of being absorbed by or occluded therein. It, therefore, is essential to the obtaming of soft, ductile, adherent deposits that all gases, and particularly hydrogen gas, be prevented from adhering to the article being coated and that the hydrogen concentration of the electrolyte be maintained substantially constant at its original concentration.
- the first step in my process of coating the inner surface of an aluminum alloy cylinder with iron is to cleanse thoroly the surface to be coated and to provide minute interstices therein into which the deposited metal can penetrate and find anchorage. I do this preferably as follows.
- the cylinder is immersed in a dilute solution of sodium hydroxide for several minutes during which time the inner surface is constantly rubbed with a softswab. Foreign substances and oxide coatings are thus removed and the surface is etched or appreciably roughened. Apparently a substantial amount of such etching is conducive to good adherence of the
- the cleaned cylinder is next dipped in a weak solution of acetic acid and rinsed with water and is then ready to be coated. If it is not to be coated immediately it may be left immersed. in the acetic acid solution where it will be protected from oxidation until transferred to the electrolyte.
- the second step of the process is the preparation of the electrolyte.
- the calculated amount of ferrous sulfate to form a saturated solution is first dissolved in water. After complete solution, ammonium hydroxide is added until the solution becomes of a thick sludge or mud-like consistenc due to the precipitation therein of iron hy roxides and probably basic iron compounds.
- the electrolyte may also be formed by adding to a saturated ferrous sulfate solution a sufficient amount of precipitated ferrous hydroxide. Ferrous chloride and other suitable iron salts may be employed instead of the ferrous sulfate above specified.
- the third and final step in the process is the actual deposition of the iron on the cylinder. It is accomplished by rotatably suspending the cylinder in the electrolyte around an iron anode and constituting it the cathode or negative terminal of an electric circuit. With an electrolyte temperature of about F., a current density of approximately .026 amperes per square decimeter at 2% volts and a speed of rotation of 250 revolutions per minute, a coating of iron will form on the cylinder which in the course of about 3 hrs. will amount to about .004 in thickness. Prolonged action or increased current density will result in a thicker coating. This coating is smooth, free from all pits or surface depression, is soft, ductile and firmly adherent to the cylinder. After a coating of the desired thickness has been deposited the cylinder is removed from the electrolyte and washed with water after which the plate may be finished to size as by grinding or otherwise.
- the precipitated substances in the electrolyte will effectively remove adhering gases from the article being coated when either the electrolyte or the article is agitated.
- the process may, accordingly, be practiced by suitably stirring the electrolyte rather than by rotating or moving the article being coated.
- the nature of the article to be coated might make it impossible to rotate or otherwise agitate the article in the electrolyte.
- 'An example is the coating of the interior surfaces of the cylinders in a cylinder block casting of an internal combustion engine.
- theelectrolyte itself may be caused to flow along and in contact with the cylinder walls by employing a pump, by suitable liquid propelling vanes on a rotating anode and by various other means.
- An electrolyte for electrolytically depositing iron composed of a ferrous sulfate solu- I tion containing precipitated iron hydroxide in suspension and having a thick mud-like consistency.
- An electrolyte for depositing metals of the iron group which is characterized by having an excess of a metallic hydroxide of a metal of the iron group permeating the entire electrolyte in an amount sufficient to prevent gases adhering to a moving cathode and also to automatically maintain the acidity of the electrolyte substantially constant.
- An electrolyte for electrolytically depositing metals of the iron group composed of a solution of a salt of the metal to be deposited and containing hydroxide of that metal in suspension and characterized by being of a thick mud-like consistency.
- a process for forming a coating of iron on metallic articles which comprises suitably preparing the article to receive an electrolytic deposit of iron, bringing the article into contact with an electrolyte characterized by containing iron hydroxide in suspension in sufficient amount to form a solution of thick mud-like consistency, and passing an electric current through the electrolyte and to the said article during relative movement of the hydroxide and article.
- a process for formin wear resisting coatings of iron on metallic articles which comprises preparing an electrolyte of mud like consistenc containing iron h droxide in suspension, 0 caning the surface 0 the article to be coated, placing the said article in the electrolyte, passing an electric current thru the electrolyte and to the said article, and causing a rubbing gas removing action of the said hydroxide against the surface to be coated while automatically maintaining substantially constant the acidity of thefelectrolyte.
- metals of the iron group on aluminum alloy articles which comprises cleanin and etching the article to be coated, providing an electrolyte of mud-like consistency carrying in suspension a hydroxide of the metal to be deposited, bringing the hydroxide and the said article into contact, and causing constant relative movement therebetween while passing a current of electricity thru the said electrolyte to said article and while maintaining substantially constant the acidity of the electrolyte.
- a bath for the electro deposition of metals of the iron group of thick mud-like consistency comprising a salt of a metal of the iron group in solution, and a finely divided hydrate of a metal of the iron group in suspension therein.
- An'electrolyte for use in the electrolytic deposition of metals of the iron group characterized by possessing'a thick, mud-like consistency and containing a solution of a salt of the metal to be de osited.
Description
Patented Oct. 1, 1929 UNITED STATES PATENT OFFICE FRED x. BEZZENBERGER, or CLEVELAND, 01110, ASSIGNOR, BY MESNE nssrenusn'rs,
'ro ALUMINUM company or AMERICA, or PITTSBURGH, rnnnsnvanm, A con- POBATION OF PENNSYLVANIA PROCESS FOR ELECTRODEPOSITION OF METAL No Drawing. Application filed July 14, 1921, Serial No. 484,785. Renewed Inns 7, 1924.
This invention relates generally to the electrolytic deposition of metals and more particularly to a process for depositing metals of the iron group on articles composed of 5 aluminum and its alloys.
One object of the invention is to provide a process by which firmly adherent and smooth coatings of metals of the iron group mayAbe cheaply and easily deposited upon electrically conductive surfacest Another object is to provide a process of depositing smooth, soft coatings of iron on articles composed of aluminum and its alloys.
Another object is to provide a new and iml5 proved electrolyte which, in addition to performing the usual functions of an ordinary electrolyte, is capable of maintaining substantially constant its initial degree of acidity or hydrogen concentration and when suitably l0 agitated, of effectively preventing adherence of gases to the surface to be coated.
Other objects, more or less ancillary to the above objects, will appear and be pointed out in the appended specification. I In electrolytically depositing iron and other metals of the iron group in which I have included iron, nickel and cobalt, I have discovered that many serious difficulties encountered heretofore, of which the more important are perhaps brittleness, pitting and lack of adherence of the deposited metal to the article upon which it is deposited, can be avoided. A preferred means of accomplishing this result and obtaining uniformly smooth, soft, ductile and adherent metallic coatings consists briefly in practicing a new and improved process of cleaning the article on which the metal is to be deposited and then electrolytically depositing the metal thereon from an electrolyte of novel composition.
Theoretically, in electroplating, the electric current liberates free acid when it deposits metal from the electrolyte and then immediately causes combination of the free acid with a corresponding amount of metal from a metal electrode thereby maintaining constant the original acidity or hydrogen concentration of the electrolyte. Practically, however, an excess of free acid tends to accumulate as the process of deposition proceeds and the increased acidity or hydrogen concentration of the electrolyte is visibly indicated by the collection on the article being coated of bubbles of gas which is mainly hydrogen.
Increased acidity or high hydrogen concentration in the electrolyte is harmful to the deposited metal since, in addition to causing pitting by adhering in bubble form to. the
article being coated, hydrogen also causes brittleness and peeling of the deposited metal by reason of being absorbed by or occluded therein. It, therefore, is essential to the obtaming of soft, ductile, adherent deposits that all gases, and particularly hydrogen gas, be prevented from adhering to the article being coated and that the hydrogen concentration of the electrolyte be maintained substantially constant at its original concentration.
Accordingly my process is adapted to avoid these harmful conditions bycontrolling automatically the hydrogen concentration in the electrolyte Within certain narrow limits and removing any adhering gases from the article being coated.
For purposes of describing my process so that those skilled in the art can practice it, I have elected to describe it more or less in detail in connection with the depostion of an iron coating on the interior surface of a cylinder composed of aluminum alloys. In doing so, however, I do not wish to be understood as limiting the scope of my invention to the details set forth.
The first step in my process of coating the inner surface of an aluminum alloy cylinder with iron is to cleanse thoroly the surface to be coated and to provide minute interstices therein into which the deposited metal can penetrate and find anchorage. I do this preferably as follows. The cylinder is immersed in a dilute solution of sodium hydroxide for several minutes during which time the inner surface is constantly rubbed with a softswab. Foreign substances and oxide coatings are thus removed and the surface is etched or appreciably roughened. Apparently a substantial amount of such etching is conducive to good adherence of the The cleaned cylinder is next dipped in a weak solution of acetic acid and rinsed with water and is then ready to be coated. If it is not to be coated immediately it may be left immersed. in the acetic acid solution where it will be protected from oxidation until transferred to the electrolyte.
. I have found that solutions of the following strengths are satisfactory for the above 111 0868. p p Per cent solution Sodium hydroxide 10 First nitric acid 20 Second nitric acid 1 Acetic acid 1 Obviously other suitable solutions may be substituted for these so utions and the strength of each solution may be altered Without departing from the spirit of my invention. It is also permissible to dispense with one or more of these solutions provided only that the article is suitably cleaned and etched and then freed from all reacting solutions and their products.
The second step of the process is the preparation of the electrolyte. The calculated amount of ferrous sulfate to form a saturated solution is first dissolved in water. After complete solution, ammonium hydroxide is added until the solution becomes of a thick sludge or mud-like consistenc due to the precipitation therein of iron hy roxides and probably basic iron compounds. The electrolyte may also be formed by adding to a saturated ferrous sulfate solution a sufficient amount of precipitated ferrous hydroxide. Ferrous chloride and other suitable iron salts may be employed instead of the ferrous sulfate above specified.
The third and final step in the process is the actual deposition of the iron on the cylinder. It is accomplished by rotatably suspending the cylinder in the electrolyte around an iron anode and constituting it the cathode or negative terminal of an electric circuit. With an electrolyte temperature of about F., a current density of approximately .026 amperes per square decimeter at 2% volts and a speed of rotation of 250 revolutions per minute, a coating of iron will form on the cylinder which in the course of about 3 hrs. will amount to about .004 in thickness. Prolonged action or increased current density will result in a thicker coating. This coating is smooth, free from all pits or surface depression, is soft, ductile and firmly adherent to the cylinder. After a coating of the desired thickness has been deposited the cylinder is removed from the electrolyte and washed with water after which the plate may be finished to size as by grinding or otherwise.
It is obvious that the precipitated substances in the electrolyte will effectively remove adhering gases from the article being coated when either the electrolyte or the article is agitated. The process may, accordingly, be practiced by suitably stirring the electrolyte rather than by rotating or moving the article being coated. For instance, the nature of the article to be coated might make it impossible to rotate or otherwise agitate the article in the electrolyte.
'An example is the coating of the interior surfaces of the cylinders in a cylinder block casting of an internal combustion engine. There theelectrolyte itself may be caused to flow along and in contact with the cylinder walls by employing a pump, by suitable liquid propelling vanes on a rotating anode and by various other means.
Altho the reactions involved in electroplating are complex, in general, I believe the reaction by which the automatic control of the acidity or the hydrogen concentration of the electrolyte is brought about are as follows: Passage of a current of electricity thru the electrolyte deposits iron on the cathode and liberates sulfuric acid. The excess acid, which is not neutralized by metallic iron from the anode, then reacts with the precipitated iron hydroxide which permeates the entire electrolyte and which is in a condition favorable to prompt reaction with anacid thus forming neutral ferrous sulfate. In this manner the original acidity or hydrogen concentration of the electrolyte is maintained substantially constant. As the use of the electrolyte is prolonged, it may, of course, become necessary to add fresh quantities of precipitated iron hydroxide at intervals to replace that used in controlling the acidity of the electrolyte.
Altho I have described my process in-some detail, as practiced on one particular article, it will be understood by those skilled in the art as being merely illustrative and that many variations in the steps of the process may be made without departing from the scope of my invention. It is also to be understood that my improved process is broadly applicable to the deposition of other metals of the iron group as above defined, and also to the deposition of such metals on articles composed of electrically conductive substances other than aluminum and its alloys.
All these modifications are comprehended by my invention, the scope of which is defined by what is claimed.
What is claimed:
1. An electrolyte for electrolytically depositing iron composed of a ferrous sulfate solu- I tion containing precipitated iron hydroxide in suspension and having a thick mud-like consistency.
2. An electrolyte for depositing metals of the iron group which is characterized by having an excess of a metallic hydroxide of a metal of the iron group permeating the entire electrolyte in an amount sufficient to prevent gases adhering to a moving cathode and also to automatically maintain the acidity of the electrolyte substantially constant.
3. An electrolyte for electrolytically depositing metals of the iron group, composed of a solution of a salt of the metal to be deposited and containing hydroxide of that metal in suspension and characterized by being of a thick mud-like consistency. I
4. A process for forming a coating of iron on metallic articles which comprises suitably preparing the article to receive an electrolytic deposit of iron, bringing the article into contact with an electrolyte characterized by containing iron hydroxide in suspension in sufficient amount to form a solution of thick mud-like consistency, and passing an electric current through the electrolyte and to the said article during relative movement of the hydroxide and article.
5. A process for formin wear resisting coatings of iron on metallic articles which comprises preparing an electrolyte of mud like consistenc containing iron h droxide in suspension, 0 caning the surface 0 the article to be coated, placing the said article in the electrolyte, passing an electric current thru the electrolyte and to the said article, and causing a rubbing gas removing action of the said hydroxide against the surface to be coated while automatically maintaining substantially constant the acidity of thefelectrolyte.
6. A process for electrolytically depositin the electrolyte during the deposition of metal on the cathode.
In testimony whereof I affix my signature. V
FRED K. BEZZENBERGER.
ing metals of the iron group on aluminum alloy articles which comprises cleanin and etching the article to be coated, providing an electrolyte of mud-like consistency carrying in suspension a hydroxide of the metal to be deposited, bringing the hydroxide and the said article into contact, and causing constant relative movement therebetween while passing a current of electricity thru the said electrolyte to said article and while maintaining substantially constant the acidity of the electrolyte.
7. A bath for the electro deposition of metals of the iron group of thick mud-like consistency comprising a salt of a metal of the iron group in solution, and a finely divided hydrate of a metal of the iron group in suspension therein.
8. An'electrolyte for use in the electrolytic deposition of metals of the iron group, characterized by possessing'a thick, mud-like consistency and containing a solution of a salt of the metal to be de osited.
9. The process of epositing metals of the
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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US484785A US1729607A (en) | 1921-07-14 | 1921-07-14 | Process for electrodeposition of metal |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US484785A US1729607A (en) | 1921-07-14 | 1921-07-14 | Process for electrodeposition of metal |
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Publication Number | Publication Date |
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US1729607A true US1729607A (en) | 1929-10-01 |
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US484785A Expired - Lifetime US1729607A (en) | 1921-07-14 | 1921-07-14 | Process for electrodeposition of metal |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2714089A (en) * | 1953-01-26 | 1955-07-26 | Enthone | Electrodepositing iron |
US5516419A (en) * | 1994-05-26 | 1996-05-14 | Hughes Aircraft Company | Hard iron plating of aluminum/aluminum alloys using sulfamate/sulfate solutions |
US6284123B1 (en) | 1998-03-02 | 2001-09-04 | Briggs & Stratton Corporation | Electroplating formulation and process for plating iron onto aluminum/aluminum alloys |
US10450658B2 (en) * | 2014-05-06 | 2019-10-22 | Case Western Reserve University | Alloy surface activation by immersion in aqueous acid solution |
-
1921
- 1921-07-14 US US484785A patent/US1729607A/en not_active Expired - Lifetime
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2714089A (en) * | 1953-01-26 | 1955-07-26 | Enthone | Electrodepositing iron |
US5516419A (en) * | 1994-05-26 | 1996-05-14 | Hughes Aircraft Company | Hard iron plating of aluminum/aluminum alloys using sulfamate/sulfate solutions |
US6284123B1 (en) | 1998-03-02 | 2001-09-04 | Briggs & Stratton Corporation | Electroplating formulation and process for plating iron onto aluminum/aluminum alloys |
US10450658B2 (en) * | 2014-05-06 | 2019-10-22 | Case Western Reserve University | Alloy surface activation by immersion in aqueous acid solution |
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