GB637714A - Improvements in and relating to the production of metal powders - Google Patents
Improvements in and relating to the production of metal powdersInfo
- Publication number
- GB637714A GB637714A GB3395345A GB3395345A GB637714A GB 637714 A GB637714 A GB 637714A GB 3395345 A GB3395345 A GB 3395345A GB 3395345 A GB3395345 A GB 3395345A GB 637714 A GB637714 A GB 637714A
- Authority
- GB
- United Kingdom
- Prior art keywords
- metal
- melt
- powder
- metals
- electrolyte
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- C25C5/00—Electrolytic production, recovery or refining of metal powders or porous metal masses
- C25C5/04—Electrolytic production, recovery or refining of metal powders or porous metal masses from melts
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electrolytic Production Of Metals (AREA)
Abstract
637,714. Electrolytic production of metal powders. JOHANSSON, E. H. E., and TRUEDSSON, C. M. Dec. 14, 1945, No. 33953. [Class 41] In the production of powder from heavy metals or alloys such as iron, nickel, chromium and copper, using anodes of the required metal, the electrolysis is carried out in a non- oxidizing atmosphere with an electrolyte comprising a melt of a salt of an alkali or alkaline earth metal or a radical which is more electropositive than the required metal, which melt does not attack the anode metal except when current is passed and which is kept at a temperature below the melting point of the metal, the required metal being present in the melt in an ionized state in a low concentration, kept constant by avoiding any oxidation and introduction of non-anodic substances which might cause an increase of the anion concentration. The melt is preferably a chloride or other halogen salt of an alkali metal, and is preferably free from oxides or other compounds of the anode metal, with the exception of the salt formed at the anode during the electrolysis. Preferably the cathode also consists of the metal or alloy to be produced in powdered form. To remove oxidizing compounds, the melt, apparatus and electrodes may be heated to redness in an atmosphere of hydrogen. During electrolysis there may be added to the electrolyte alkali or alkaline earth metals which vaporize and thus prevent oxidation ; alternatively, mixtures which liberate these metals may be added. To prevent short-circuiting by liquid metal floating on the electrolyte, these added metals may be contained in tubes having openings controlled in such a way that only vapour can escape to the region above the electrolyte. The vapour may be expelled from the tubes by an inert gas. To prevent sintering of the powder produced, the temperature in the space below the electrodes where the powder collects may be kept low by extending the vessel downwards and by using a low-melting point melt. A coarser powder is produced if halogen salts, preferably fluorides of the anode metal or metals, preferably mixed with alkali metal fluorides, are added to the melt. For the production of iron powder the electrolyser consists of outer and inner vessels 1, 2, the space between them being filled by a non-oxidizing gas such as hydrogen led in at 4 and out at 4<1>. In an annular lid 3, tubes 6 are provided for introducing gases or vapours to drive out the air and prevent oxidation. A cylindrical skirt 3<1> depending from the lid 3 is closed by a circular lid 5, provided with further pipes 6<1>. The vessel, including the skirt 3<1>, is made the cathode, and scrapers 7 are provided for removing the powder from the vertical surfaces as it is formed. A scraper 9 is provided. There may be a plurality of cylindrical extensions 3<1> serving as cathodes. The electrolysis may be carried out with a diaphragm between the cathode and anodes 8.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB3395345A GB637714A (en) | 1945-12-14 | 1945-12-14 | Improvements in and relating to the production of metal powders |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB3395345A GB637714A (en) | 1945-12-14 | 1945-12-14 | Improvements in and relating to the production of metal powders |
Publications (1)
Publication Number | Publication Date |
---|---|
GB637714A true GB637714A (en) | 1950-05-24 |
Family
ID=10359521
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB3395345A Expired GB637714A (en) | 1945-12-14 | 1945-12-14 | Improvements in and relating to the production of metal powders |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB637714A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2786808A (en) * | 1954-09-22 | 1957-03-26 | Chicago Dev Corp | Production of titanium |
US2831802A (en) * | 1951-11-14 | 1958-04-22 | Chicago Dev Corp | Production of subdivided metals |
US2864749A (en) * | 1951-05-09 | 1958-12-16 | Timax Corp | Process for the production of titanium metal |
DE1096617B (en) * | 1954-07-06 | 1961-01-05 | New Jersey Zinc Co | Process for the electrolytic production of titanium |
-
1945
- 1945-12-14 GB GB3395345A patent/GB637714A/en not_active Expired
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2864749A (en) * | 1951-05-09 | 1958-12-16 | Timax Corp | Process for the production of titanium metal |
US2831802A (en) * | 1951-11-14 | 1958-04-22 | Chicago Dev Corp | Production of subdivided metals |
DE1096617B (en) * | 1954-07-06 | 1961-01-05 | New Jersey Zinc Co | Process for the electrolytic production of titanium |
US2786808A (en) * | 1954-09-22 | 1957-03-26 | Chicago Dev Corp | Production of titanium |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US2734856A (en) | Electrolytic method for refining titanium metal | |
Senderoff et al. | The electrolytic preparation of molybdenum from fused salts: I. Electrolytic studies | |
JP5469042B2 (en) | Method for electrically producing alkali metal from alkali metal amalgam | |
US3114685A (en) | Electrolytic production of titanium metal | |
GB833767A (en) | Continuous electrolytic production of titanium | |
UA65558C2 (en) | A process for the electrolytic production of metals | |
US20170159193A1 (en) | Method and apparatus for electrolytic reduction of a feedstock comprising oxygen and a first metal | |
GB635267A (en) | Improvements in and relating to the production of metals by electrolysis in a fused bath | |
US2302604A (en) | Fused bath electrolytic production of ferrochromium | |
GB734094A (en) | A new or improved process for the production of refractory metals | |
US2848397A (en) | Electrolytic production of metallic titanium | |
GB678807A (en) | Process for the production of titanium metal | |
GB637714A (en) | Improvements in and relating to the production of metal powders | |
US2734855A (en) | Electrolytic preparation of reduced | |
US3137641A (en) | Electrolytic process for the production of titanium metal | |
US2655473A (en) | Electrolytic detinning | |
US2892763A (en) | Production of pure elemental silicon | |
US2939823A (en) | Electrorefining metallic titanium | |
US2887443A (en) | Arc-cathode production of titanium | |
US2913382A (en) | Method for producing metals electrolytically | |
GB626636A (en) | Improvements in and relating to the production of powder or sponge of metals or metal alloys by electrolytic reduction of metal oxides or other reducible metal compounds | |
GB1199038A (en) | Improvements in process for Nickeliding, Cobaltiding and Ironiding Base Metal Compositions | |
Kovrov et al. | Anodic behavior of the NiO-Fe 2 O 3-Cr 2 O 3-Cu composite during the low-temperature electrolysis of aluminum | |
US2952591A (en) | Electrolytic preparation of calcium carbide | |
Piper et al. | Electrolytic production of uranium metal from uranium oxides |