GB741630A - Process for the production of metals by reduction of their halides - Google Patents

Process for the production of metals by reduction of their halides

Info

Publication number
GB741630A
GB741630A GB19781/53A GB1978153A GB741630A GB 741630 A GB741630 A GB 741630A GB 19781/53 A GB19781/53 A GB 19781/53A GB 1978153 A GB1978153 A GB 1978153A GB 741630 A GB741630 A GB 741630A
Authority
GB
United Kingdom
Prior art keywords
metal
halide
vapour
silicon
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
GB19781/53A
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.)
Evonik Operations GmbH
Original Assignee
Degussa GmbH
Deutsche Gold und Silber Scheideanstalt
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 Degussa GmbH, Deutsche Gold und Silber Scheideanstalt filed Critical Degussa GmbH
Publication of GB741630A publication Critical patent/GB741630A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B34/00Obtaining refractory metals

Abstract

Silicon is produced by introducing the vapour of a halide of silicon, having an absolute heat of formation not exceeding 70 kilogram calories per gram atom of halogen present in the halide, and the vapour of a reducing metal which is an alkali metal or magnesium in a single, constricted, vaporous stream into a reaction chamber which is evacuated or filled with an inert gas, igniting the stream and impinging the flame upon a collecting surface maintained at a temperature below the boiling point of the silicon and above the boiling point of the reducing metal halide. The reducing metal is preferably sodium. The silicon halide vapour and the reducing metal vapour may be introduced into the reaction chamber through a common nozzle opening, preceded by a mixing chamber, or through two concentric nozzles and additional heat may be supplied to the reaction by heating one or both reactants. The collecting surface may be concave and kept at a temperature above or below the melting point of the collected silicon or may be tubular and the silicon continuously discharged, e.g., in liquid form, from the reaction chamber. Alternatively, by controlled heat dissipation from the collecting surface, the surface only of the collected silicon may be kept molten and the solidified silicon continuously withdrawn from the chamber. Additional heat may be supplied to the collecting surface by electric gas discharge, e.g., an electric arc, the discharge also serving to heat the vaporous reactants. Separate auxiliary electrodes may be provided to maintain the arc or the common nozzle on the surface of the collected metal may be used as electrodes. The vaporous reducing metal halide may be condensed in the reaction chamber or after removal as vapour therefrom.ALSO:Metals, e.g. Ti, Zr, V, W and Mo, are produced by introducing the vapour of a halide of the metal, having an absolute heat of formation not exceeding 70 kilogram calories per gram atom of halogen present in the halide, and the vapour of a reducing metal which is an alkali metal or magnesium in a single, constricted, vaporous stream into a reaction chamber which is evacuated or filled with an inert gas, igniting the stream and impinging the flame upon a collecting surface maintained at a temperature below the boiling point of the required metal and above the boiling point of the reducing metal halide. The reducing metal is preferably sodium. The metal halide vapour and the reducing metal vapour may be introduced into the reaction chamber through a common nozzle opening, preceded by a mixing chamber, or through two concentric nozzles and additional heat may be supplied to the reaction by heating one or both reactants. The collecting surface may be concave and kept at a temperature above or below the melting point of the collected metal or may be tubular and metal continuously discharged, e.g. in liquid form, from the reaction chamber. Alternatively, by controlled heat dissipation from the collecting surface, the surface only of the collected metal may be kept molten and the solidified metal continuously withdrawn from the chamber. Additional heat may be supplied to the collecting surface by electric gas discharge, e.g. an electric arc, the discharge also serving to heat the vaporous reactants. Separate auxiliary electrodes may be provided to maintain the arc or the common nozzle or the surface of the collected metal may be used as electrodes. The vaporous reducing metal halide may be condensed in the reaction chamber or after removal as vapour therefrom. Using two or more metal halides, alloys may be produced and, using a silicon halide with one or more metal halides, alloys containing silicon may be produced.
GB19781/53A 1952-07-17 1953-07-16 Process for the production of metals by reduction of their halides Expired GB741630A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE741630X 1952-07-17

Publications (1)

Publication Number Publication Date
GB741630A true GB741630A (en) 1955-12-07

Family

ID=6644959

Family Applications (1)

Application Number Title Priority Date Filing Date
GB19781/53A Expired GB741630A (en) 1952-07-17 1953-07-16 Process for the production of metals by reduction of their halides

Country Status (1)

Country Link
GB (1) GB741630A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3041145A (en) * 1957-07-15 1962-06-26 Robert S Aries Production of pure silicon
US4830665A (en) * 1979-07-05 1989-05-16 Cockerill S.A. Process and unit for preparing alloyed and non-alloyed reactive metals by reduction
US5021221A (en) * 1980-10-20 1991-06-04 Aero Chem Research Lab., Inc. Apparatus for producing high purity silicon from flames of sodium and silicon tetrachloride

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3041145A (en) * 1957-07-15 1962-06-26 Robert S Aries Production of pure silicon
US4830665A (en) * 1979-07-05 1989-05-16 Cockerill S.A. Process and unit for preparing alloyed and non-alloyed reactive metals by reduction
US5021221A (en) * 1980-10-20 1991-06-04 Aero Chem Research Lab., Inc. Apparatus for producing high purity silicon from flames of sodium and silicon tetrachloride

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