GB386621A - Improved process for alloying or combining metals of any kind - Google Patents
Improved process for alloying or combining metals of any kindInfo
- Publication number
- GB386621A GB386621A GB10864/31A GB1086431A GB386621A GB 386621 A GB386621 A GB 386621A GB 10864/31 A GB10864/31 A GB 10864/31A GB 1086431 A GB1086431 A GB 1086431A GB 386621 A GB386621 A GB 386621A
- Authority
- GB
- United Kingdom
- Prior art keywords
- metal
- reaction
- beryllium
- gases
- reaction chamber
- 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
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C1/00—Making non-ferrous alloys
- C22C1/02—Making non-ferrous alloys by melting
- C22C1/03—Making non-ferrous alloys by melting using master alloys
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
A process for the production of alloys, or combinations of metals of any kind, consists in separating a metal from its combination with an acid radical consisting of one kind of atom, e.g. a halide, by a second metal which is to be alloyed with the first metal, the second metal entering into a volatile combination with the acid radical of the first metal compound. If a chloride of the first metal is to be reduced it may be prepared by the direct chlorination of the raw ore. In an example, beryllium chloride vapour is fed into a receptacle containing aluminium. Aluminium chloride is formed and escapes with some unreduced beryllium chloride from the reaction chamber, the reduced beryllium alloying with the excess of aluminium on the application of more heat. The beryllium particles liberated may be fused together instead of being alloyed with an excess of aluminium. The working conditions may be so chosen that the salt to be decomposed is partly solid in the reaction chamber, and the yield of reduced metal may be controlled by adjusting the conditions of temperature and pressure. The reaction may take place in currents of gases which are inert towards, or which participate partly or completely in, the reaction, e.g. nitrogen, hydrogen, or rare gases such as argon, etc.; and such gases may serve to distil metals such as aluminium, magnesium, &c., into the reaction chamber, or to render non-volatile compounds produced by the reaction volatile during the process, as when beryllium sulphide is reduced in hydrogen, hydrogen sulphide being formed leaving the beryllium in the chamber to alloy with the second metal. Similar reactions occur with azides when hydrogen is used. The working temperature may be so arranged that the formation of the alloy takes place substantially or completely at the temperature of the reduction without additional heating. Heat for the initiation of the reduction and for its maintenance and for the alloying process may be supplied externally or by such means as the gases used in the process. The heat of the gases leaving the reaction chamber may be utilized by leading the gases around the reaction chamber. To utilize fully the heat developed during the reaction the walls of the reaction chamber are made of suitable material such as oxides of the metals taking part in the reaction, gold, platinum, iron, or nickel, or the walls may be plated with gold, platinum, &c.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE386621X | 1930-04-17 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB386621A true GB386621A (en) | 1933-01-19 |
Family
ID=6371004
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB10864/31A Expired GB386621A (en) | 1930-04-17 | 1931-04-13 | Improved process for alloying or combining metals of any kind |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB386621A (en) |
Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2744006A (en) * | 1951-11-08 | 1956-05-01 | Du Pont | Method of producing refractory metals |
US2745735A (en) * | 1953-04-28 | 1956-05-15 | Kaiser Aluminium Chem Corp | Method of producing titanium |
US2766113A (en) * | 1953-02-11 | 1956-10-09 | Dow Chemical Co | Method of making titanium alloys |
US2772875A (en) * | 1953-02-18 | 1956-12-04 | Levy Joseph Peppo | Production of pure titanium and zirconium |
US2791499A (en) * | 1953-07-13 | 1957-05-07 | Ethyl Corp | Method of reducing refractory metal compounds |
US2827371A (en) * | 1951-11-01 | 1958-03-18 | Ici Ltd | Method of producing titanium in an agitated solids bed |
US2830893A (en) * | 1954-04-06 | 1958-04-15 | Chicago Dev Corp | Processes for making titanium |
US2840465A (en) * | 1952-10-20 | 1958-06-24 | Dow Chemical Co | Method of producing titanium |
US2843477A (en) * | 1953-12-03 | 1958-07-15 | Du Pont | Method of producing titanium |
US2870007A (en) * | 1952-07-17 | 1959-01-20 | Degussa | Process for the production of metals by reduction of their compounds in the vapor phase |
US2882144A (en) * | 1955-08-22 | 1959-04-14 | Allied Chem | Method of producing titanium |
US3004848A (en) * | 1958-10-02 | 1961-10-17 | Nat Distillers Chem Corp | Method of making titanium and zirconium alloys |
US3020151A (en) * | 1957-02-26 | 1962-02-06 | John S Nachtman | Beneficiation and recovery of metals |
US3157493A (en) * | 1962-01-22 | 1964-11-17 | Cons Mining & Smelting Co | Production of niobium |
US3216822A (en) * | 1962-02-28 | 1965-11-09 | Wyandotte Chemicals Corp | Production of niobium by vapor phase reduction of niobium pentachloride |
-
1931
- 1931-04-13 GB GB10864/31A patent/GB386621A/en not_active Expired
Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2827371A (en) * | 1951-11-01 | 1958-03-18 | Ici Ltd | Method of producing titanium in an agitated solids bed |
US2744006A (en) * | 1951-11-08 | 1956-05-01 | Du Pont | Method of producing refractory metals |
US2870007A (en) * | 1952-07-17 | 1959-01-20 | Degussa | Process for the production of metals by reduction of their compounds in the vapor phase |
US2840465A (en) * | 1952-10-20 | 1958-06-24 | Dow Chemical Co | Method of producing titanium |
US2766113A (en) * | 1953-02-11 | 1956-10-09 | Dow Chemical Co | Method of making titanium alloys |
US2772875A (en) * | 1953-02-18 | 1956-12-04 | Levy Joseph Peppo | Production of pure titanium and zirconium |
US2745735A (en) * | 1953-04-28 | 1956-05-15 | Kaiser Aluminium Chem Corp | Method of producing titanium |
US2791499A (en) * | 1953-07-13 | 1957-05-07 | Ethyl Corp | Method of reducing refractory metal compounds |
US2843477A (en) * | 1953-12-03 | 1958-07-15 | Du Pont | Method of producing titanium |
US2830893A (en) * | 1954-04-06 | 1958-04-15 | Chicago Dev Corp | Processes for making titanium |
US2882144A (en) * | 1955-08-22 | 1959-04-14 | Allied Chem | Method of producing titanium |
US3020151A (en) * | 1957-02-26 | 1962-02-06 | John S Nachtman | Beneficiation and recovery of metals |
US3004848A (en) * | 1958-10-02 | 1961-10-17 | Nat Distillers Chem Corp | Method of making titanium and zirconium alloys |
US3157493A (en) * | 1962-01-22 | 1964-11-17 | Cons Mining & Smelting Co | Production of niobium |
US3216822A (en) * | 1962-02-28 | 1965-11-09 | Wyandotte Chemicals Corp | Production of niobium by vapor phase reduction of niobium pentachloride |
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