GB386621A - Improved process for alloying or combining metals of any kind - Google Patents

Improved process for alloying or combining metals of any kind

Info

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
Application number
GB10864/31A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Publication of GB386621A publication Critical patent/GB386621A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C1/00Making non-ferrous alloys
    • C22C1/02Making non-ferrous alloys by melting
    • C22C1/03Making non-ferrous alloys by melting using master alloys

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.
GB10864/31A 1930-04-17 1931-04-13 Improved process for alloying or combining metals of any kind Expired GB386621A (en)

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)

* Cited by examiner, † Cited by third party
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

Cited By (15)

* Cited by examiner, † Cited by third party
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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