US2499808A - Process for electroplating molybdenum and molybdenum alloys - Google Patents
Process for electroplating molybdenum and molybdenum alloys Download PDFInfo
- Publication number
- US2499808A US2499808A US456821A US45682142A US2499808A US 2499808 A US2499808 A US 2499808A US 456821 A US456821 A US 456821A US 45682142 A US45682142 A US 45682142A US 2499808 A US2499808 A US 2499808A
- Authority
- US
- United States
- Prior art keywords
- molybdenum
- electrolyte
- cathode
- electroplating
- current density
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- 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
- C25D3/56—Electroplating: Baths therefor from solutions of alloys
-
- 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
- C25D3/54—Electroplating: Baths therefor from solutions of metals not provided for in groups C25D3/04 - C25D3/50
Definitions
- the invention relates to the electrodeposition of molybdenum.
- molybdenum may be efliciently electrodeposited from aqueous electrolytes containing molybdic acid, its anhydride or its salts in the presence of the fluoride ion.
- the work on which the electrodeposition of molybdenum is desired is placed in the electrolyte to form the cathode and the anode is a conducting material which will not be attacked by the reaction products at the anode such as carbon.
- the deposited metal is resistant to acid such as cold hydrochloric and sulfuric and is resistant to strong alkalies, but is soluble in nitric acid.
- Alloys of mixtures of molybdenum with other metals may be prepared by codenosition.
- To prepare an iron alloy or mixture 5 cc. of a solution of ferrous sulfate, FeSO4, containing 0.02 gram of the element iron per cc., is added to the electrolyte.
- To prepare a nickel alloy 3 cc. of a solution of nickel sulfate, NiSO4, containing 0.02 gram of the element nickel per cc., is added to the electrolyte.
- To prepare a cobalt alloy 3 cc. of a solution of cobalt sulfate, C0804, containing 0.02 gram of the element cobalt per cc., is added to the electrolyte.
- Our process is adapted for the electroplating of articles with molybdenum or with alloys of molybdenum with other metals to render them corrosion-resistant as well as to obtain a bright decorative effect. It is also useful for preparing molybdenum sheet by obtaining a thick deposit of the metal on a suitable cathode and subsequently dissolving off the cathode and leaving the molybdenum in sheet form.
- the fluoride ion which is present in high concentration increases the solubility of the hexavalent molybdenum compounds in the acid solution and also, with the hydrofluoric acid, in creases the solubility of the reduction products of the hexavalent molybdenum compounds formed during the process of electrolysis, thereby preventing the precipitation of molybdenum hydroxide or basic salts.
- molybdenum compounds used are the most readily available compounds of the element.
- Molybdic anhydride, M003. and ammonium paramolybdate, (NI-I4) e-MovOnlHzO, are both commercially available and are both operative in our process.
- An electrolyte is made up of the following composition:
- molybdic anhydride 100 g. @21120 13.5 cc. HF (48%)
- the optimum conditions for obtaining deposition of molybdenum from this bath are cathode current density 0.3 ampere per square centimeter; temperature 30 to C.
- Bright metallic deposits oi molybdenum are obtained in five minutes.
- the weight of the average deposit is 0.7 mg. on an area of 12 square centimeters of cathode surface.
- the current density range for bright metal plating from this bath is from 0.2 to 0.4
- An electrolyte is made up of the following composition:
- the optimum conditions for obtaining deposits containing molybdenum and iron from this bath are; cathode current density 0.2 ampere per square centimeter; temperature 30 to 50 C. 'Bri'ght metallic plates are obtained in five minutes. The weight of an average deposit i 0.9 mg. on an area of 12 square centimeters of cathode surface. The current density range for bright metal plating from this bath is from 0.2 to 0.35 ampere per square centimeters.
- Example III An electrolyte is made up of the following composition:
- the optimum conditions for obtaining deposits containing molybdenum and cobalt are; cathode current density 0.2 ampere per square centimeter; temperature 30 to 50 C. Bright metallic plates are obtained in five minutes. The weight of an average deposit is 2.4 mg. on on area of 12 square centimeters of cathode surface. The current density range for bright metal plating from this bath is from 0.2 to 0.3 ampere per square centimeter.
- Example IV An electrolyte is made up of the following composition:
- cathode current density 0.2 ampere per square centimeter; temperature 30 C. to 50 C.
- Bright metallic plates are obtained in five minutes.
- the weight of the average deposit is 1.5 mg. on an 'area of 12 square centimeters of cathode surface.
- the current density range for bright metal plat- "ing from this bath is from 0.2 to 0.3 ampere per molybdenum comprising an aqueous solution of a molybdate compound, a concentration of fluoride ion at least several times greater than said molybdate compound and a soluble salt of a metal of the class consisting of iron, nickel and cobalt.
- the process of electroplating metallic molybdenum which comprises passing a current between an anode and the work to be plated as a cathode in an electrolyte comprising an aqueous solution of a molybdate compound of the class consisting of molybdic acid, its anhydride, and its salts, and a concentration of fluoride ion at least several times the concentration of said molybdate compound, at a temperature between room temperature and 65 C. and maintaining the current density between 0.2 and 0.4 ampere per square centimeter.
- the process of electrodepositing molybdenum alloys which comprises passing a current between an anode and the work to be plated as a cathode in an electrolyte comprising an aqueous solution of a molybdate compound of the class consisting of molybdic acid, its anhydride, and its salts, a concentration of fluoride ion at least several times the concentration of said molybdate compound and a soluble salt of a metal to be codeposited with molybdenum of the class consisting of iron, nickel, and cobalt, at a temperature between room temperature and 65 C. and maintaining the current density between 0.2 and 0.4 ampere per square centimeter.
- aqueous electrolyte containing the following ingredients in proportions on the order of 5 grams molybdic anhydride, grams potassium fluoride, and 13 cubic centimeters of 48% hydrofluoric acid.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electroplating And Plating Baths Therefor (AREA)
Description
Patented Mar. 7, 1950 PROCESS FOR ELECTROPLATING MOLYB- DENUM AND MOLYBDENUM ALLOYS Leonard F. Yntema, Webster Groves, and Mary Joecile Ksycki, St. Louis, Mo., assignors to president and board of trustees of St. Louis University, St. Louis, M0.
N Drawing. Application August 31, 1942, Serial No. 456,821
8 Claims.
The invention relates to the electrodeposition of molybdenum.
We have discovered that molybdenum may be efliciently electrodeposited from aqueous electrolytes containing molybdic acid, its anhydride or its salts in the presence of the fluoride ion.
The work on which the electrodeposition of molybdenum is desired is placed in the electrolyte to form the cathode and the anode is a conducting material which will not be attacked by the reaction products at the anode such as carbon.
been able to obtain smooth, bright, adherent deposits of molybdenum in five minutes. The deposited metal is resistant to acid such as cold hydrochloric and sulfuric and is resistant to strong alkalies, but is soluble in nitric acid.
Alloys of mixtures of molybdenum with other metals may be prepared by codenosition. To prepare an iron alloy or mixture, 5 cc. of a solution of ferrous sulfate, FeSO4, containing 0.02 gram of the element iron per cc., is added to the electrolyte. To prepare a nickel alloy, 3 cc. of a solution of nickel sulfate, NiSO4, containing 0.02 gram of the element nickel per cc., is added to the electrolyte. To prepare a cobalt alloy, 3 cc. of a solution of cobalt sulfate, C0804, containing 0.02 gram of the element cobalt per cc., is added to the electrolyte.
Our process is adapted for the electroplating of articles with molybdenum or with alloys of molybdenum with other metals to render them corrosion-resistant as well as to obtain a bright decorative effect. It is also useful for preparing molybdenum sheet by obtaining a thick deposit of the metal on a suitable cathode and subsequently dissolving off the cathode and leaving the molybdenum in sheet form.
' amples are given:
The fluoride ion which is present in high concentration increases the solubility of the hexavalent molybdenum compounds in the acid solution and also, with the hydrofluoric acid, in creases the solubility of the reduction products of the hexavalent molybdenum compounds formed during the process of electrolysis, thereby preventing the precipitation of molybdenum hydroxide or basic salts.
One of the chief advantages of our process is that the molybdenum compounds used are the most readily available compounds of the element. Molybdic anhydride, M003. and ammonium paramolybdate, (NI-I4) e-MovOnlHzO, are both commercially available and are both operative in our process.
To illustrate our invention, the following ex- Emample I An electrolyte is made up of the following composition:
5 g. molybdic anhydride 100 g. @21120 13.5 cc. HF (48%) The optimum conditions for obtaining deposition of molybdenum from this bath are cathode current density 0.3 ampere per square centimeter; temperature 30 to C. Bright metallic deposits oi molybdenum are obtained in five minutes. The weight of the average deposit is 0.7 mg. on an area of 12 square centimeters of cathode surface. The current density range for bright metal plating from this bath is from 0.2 to 0.4
ampere per square centimeter.
Ewample II An electrolyte is made up of the following composition:
2.5 g. molybdic anhydride 50 g. KF.2H2O
6.5 cc. HF (48%) 5 cc. FeSOr solution (0.02 g. Fe per cc.)
The optimum conditions for obtaining deposits containing molybdenum and iron from this bath are; cathode current density 0.2 ampere per square centimeter; temperature 30 to 50 C. 'Bri'ght metallic plates are obtained in five minutes. The weight of an average deposit i 0.9 mg. on an area of 12 square centimeters of cathode surface. The current density range for bright metal plating from this bath is from 0.2 to 0.35 ampere per square centimeters.
Example III An electrolyte is made up of the following composition:
2.5 g. molybdic anhydride 50 g. KF.2H2O 6.5 cc. HF (48%) 65 cc. H20 3 cc. C0804 solution (0.02 g. per cc.)
The optimum conditions for obtaining deposits containing molybdenum and cobalt are; cathode current density 0.2 ampere per square centimeter; temperature 30 to 50 C. Bright metallic plates are obtained in five minutes. The weight of an average deposit is 2.4 mg. on on area of 12 square centimeters of cathode surface. The current density range for bright metal plating from this bath is from 0.2 to 0.3 ampere per square centimeter. I
Example IV An electrolyte is made up of the following composition:
g. molybdic anhydride 50 g. KF.2H2O
6.5 cc. HF (48%) .65 cc. H .3 cc. NiSO;z solution (0.02 g. Ni per cc.)
The optimum conditions for obtaining deposits containing molybdenum and nickel are;
cathode current density 0.2 ampere per square centimeter; temperature 30 C. to 50 C. Bright metallic plates are obtained in five minutes. The weight of the average deposit is 1.5 mg. on an 'area of 12 square centimeters of cathode surface.
The current density range for bright metal plat- "ing from this bath is from 0.2 to 0.3 ampere per molybdenum comprising an aqueous solution of a molybdate compound, a concentration of fluoride ion at least several times greater than said molybdate compound and a soluble salt of a metal of the class consisting of iron, nickel and cobalt.
3. The process of electroplating metallic molybdenum which comprises passing a current between an anode and the work to be plated as a cathode in an electrolyte comprising an aqueous solution of a molybdate compound of the class consisting of molybdic acid, its anhydride, and its salts, hydrofluoric acid and an alkali fluoride, the concentration of the fluoride ion in said electrolyte being at least several times the concentration of said molybdate compound, at a temperature from room temperature to C. and maintaining the current density between 0.2 and 0.4 ampere per square centimeter.
4. The process according to claim 3 in which the temperature is maintained between 30 and 50 C.
5. The process of electroplating metallic molybdenum which comprises passing a current between an anode and the work to be plated as a cathode in an electrolyte comprising an aqueous solution of a molybdate compound of the class consisting of molybdic acid, its anhydride, and its salts, and a concentration of fluoride ion at least several times the concentration of said molybdate compound, at a temperature between room temperature and 65 C. and maintaining the current density between 0.2 and 0.4 ampere per square centimeter.
6. The process of electrodepositing molybdenum alloys which comprises passing a current between an anode and the work to be plated as a cathode in an electrolyte comprising an aqueous solution of a molybdate compound of the class consisting of molybdic acid, its anhydride, and its salts, a concentration of fluoride ion at least several times the concentration of said molybdate compound and a soluble salt of a metal to be codeposited with molybdenum of the class consisting of iron, nickel, and cobalt, at a temperature between room temperature and 65 C. and maintaining the current density between 0.2 and 0.4 ampere per square centimeter.
'7. An aqueous electrolyte containing the following ingredients in proportions on the order of 5 grams molybdic anhydride, grams potassium fluoride, and 13 cubic centimeters of 48% hydrofluoric acid.
8. The process of electroplating metallic molybdenum which comprises passing a current between an anode and the work to be plated as a cathode in an aqueous electrolyte containing the following ingredients in proportions on the order of 5 grams molybdic anhydride, 100 grams potassium fluoride, and 13 cubic centimeters of 48% hydrofluoric acid at a temperature between 30 and 50 C. and maintaining the current density between 0.2 and 0.4 ampere per square centimeter.
LEONARD F. YNTEMA. MARY JOECILE KSYCIU.
REFERENCES CITED The following references are of record in the file of this patent:
Chemical Abstracts, volume 35 1941), 1326 Journal of the American Chemical Society 54 (1932), pages 3775, 3776.
Claims (1)
1. AN ELECTROLYTE FOR THE ELECTRODEPOSITION OF MOLYBDENUM COMPRISING AN AQUEOUS SOLUTION OF A MOLYBDATE COMPOUND AND A CONCENTRATION OF FLUORIDE ION AT LEAST SEVERAL TIMES GREATER THAN SAID MOLYBDATE COMPOUND.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US456821A US2499808A (en) | 1942-08-31 | 1942-08-31 | Process for electroplating molybdenum and molybdenum alloys |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US456821A US2499808A (en) | 1942-08-31 | 1942-08-31 | Process for electroplating molybdenum and molybdenum alloys |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2499808A true US2499808A (en) | 1950-03-07 |
Family
ID=23814272
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US456821A Expired - Lifetime US2499808A (en) | 1942-08-31 | 1942-08-31 | Process for electroplating molybdenum and molybdenum alloys |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2499808A (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2995479A (en) * | 1961-08-08 | Degassing aluminum articles | ||
| US20070093006A1 (en) * | 2005-10-24 | 2007-04-26 | Basol Bulent M | Technique For Preparing Precursor Films And Compound Layers For Thin Film Solar Cell Fabrication And Apparatus Corresponding Thereto |
| US20070145507A1 (en) * | 2005-11-02 | 2007-06-28 | Basol Bulent M | Contact Layers For Thin Film Solar Cells Employing Group IBIIIAVIA Compound Absorbers |
| US20080023059A1 (en) * | 2006-07-25 | 2008-01-31 | Basol Bulent M | Tandem solar cell structures and methods of manufacturing same |
| CN102534655A (en) * | 2012-02-21 | 2012-07-04 | 西安建筑科技大学 | Method for electrochemically recycling and purifying molybdenum |
| EP3197246A1 (en) * | 2012-04-27 | 2017-07-26 | Triumf | Target and apparatus for cyclotron production of technetium-99m |
-
1942
- 1942-08-31 US US456821A patent/US2499808A/en not_active Expired - Lifetime
Non-Patent Citations (1)
| Title |
|---|
| None * |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2995479A (en) * | 1961-08-08 | Degassing aluminum articles | ||
| US20070093006A1 (en) * | 2005-10-24 | 2007-04-26 | Basol Bulent M | Technique For Preparing Precursor Films And Compound Layers For Thin Film Solar Cell Fabrication And Apparatus Corresponding Thereto |
| US20100229940A1 (en) * | 2005-10-24 | 2010-09-16 | Basol Bulent M | Technique for preparing precursor films and compound layers for thin film solar cell fabrication and apparatus corresponding thereto |
| US20070145507A1 (en) * | 2005-11-02 | 2007-06-28 | Basol Bulent M | Contact Layers For Thin Film Solar Cells Employing Group IBIIIAVIA Compound Absorbers |
| US7713773B2 (en) | 2005-11-02 | 2010-05-11 | Solopower, Inc. | Contact layers for thin film solar cells employing group IBIIIAVIA compound absorbers |
| WO2007108932A2 (en) * | 2006-03-13 | 2007-09-27 | Solopower, Inc. | Technique for preparing precursor films and compound layers for thin film solar cell fabrication and apparatus corresponding thereto |
| WO2007108932A3 (en) * | 2006-03-13 | 2008-10-09 | Solopower Inc | Technique for preparing precursor films and compound layers for thin film solar cell fabrication and apparatus corresponding thereto |
| US20080023059A1 (en) * | 2006-07-25 | 2008-01-31 | Basol Bulent M | Tandem solar cell structures and methods of manufacturing same |
| CN102534655A (en) * | 2012-02-21 | 2012-07-04 | 西安建筑科技大学 | Method for electrochemically recycling and purifying molybdenum |
| EP3197246A1 (en) * | 2012-04-27 | 2017-07-26 | Triumf | Target and apparatus for cyclotron production of technetium-99m |
| EP3461240B1 (en) * | 2012-04-27 | 2022-11-16 | Triumf Inc. | Processes, systems, and apparatus for cylotron production of technetium-99m |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US2653128A (en) | Method of and bath for electrodepositing tungsten alloys | |
| US2432893A (en) | Electrodeposition of nickeltungsten alloys | |
| US2693444A (en) | Electrodeposition of chromium and alloys thereof | |
| US2027358A (en) | Electrodeposition of metals of the platinum group | |
| US2499808A (en) | Process for electroplating molybdenum and molybdenum alloys | |
| US2990343A (en) | Chromium alloy plating | |
| US4115211A (en) | Process for metal plating on aluminum and aluminum alloys | |
| US2550449A (en) | Electrodeposition of nickel from an acid bath | |
| US2287654A (en) | Copper plating | |
| US3093556A (en) | Electro-depositing stainless steel coatings on metal surfaces | |
| US2493092A (en) | Method of electrodepositing copper and baths therefor | |
| US2946728A (en) | Adherent electroplating on titanium | |
| US4111760A (en) | Method and electrolyte for the electrodeposition of cobalt and cobalt-base alloys in the presence of an insoluble anode | |
| US2793990A (en) | Electrodeposition of alloys containing copper and tin | |
| US2432894A (en) | Electrodeposition of iron-tungsten alloys | |
| US1590170A (en) | Process of plating with chromium | |
| JPWO2019117230A1 (en) | Trivalent chromium plating solution and trivalent chromium plating method using this | |
| Sasaki et al. | Three crystalline modifications of electrolytic chromium | |
| McElwee et al. | The Electrodeposition of Cobalt‐Tungsten‐Molybdenum Alloys from Aqueous Citrate Solutions | |
| US2499807A (en) | Process for electroplating molybdenum and its alloys | |
| US2871173A (en) | Method of making ductile copper platings | |
| US1681509A (en) | Cadmium plating | |
| US2739108A (en) | Electroplating chromium-nickel alloy coatings | |
| US2428404A (en) | Electrodeposition of molybdenumcobalt alloys | |
| US3374156A (en) | Electro-depositing stainless steel coatings on metal surfaces |