GB867871A - Improvements in or relating to the preparation of elemental silicon - Google Patents

Improvements in or relating to the preparation of elemental silicon

Info

Publication number
GB867871A
GB867871A GB2223557A GB2223557A GB867871A GB 867871 A GB867871 A GB 867871A GB 2223557 A GB2223557 A GB 2223557A GB 2223557 A GB2223557 A GB 2223557A GB 867871 A GB867871 A GB 867871A
Authority
GB
United Kingdom
Prior art keywords
silicon
halide
vapour
purified
cadmium
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
GB2223557A
Inventor
Carl Marcus Olson
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.)
EIDP Inc
Original Assignee
EI Du Pont de Nemours and Co
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 EI Du Pont de Nemours and Co filed Critical EI Du Pont de Nemours and Co
Priority to GB2223557A priority Critical patent/GB867871A/en
Publication of GB867871A publication Critical patent/GB867871A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B33/00Silicon; Compounds thereof
    • C01B33/02Silicon
    • C01B33/021Preparation
    • C01B33/027Preparation by decomposition or reduction of gaseous or vaporised silicon compounds other than silica or silica-containing material
    • C01B33/033Preparation by decomposition or reduction of gaseous or vaporised silicon compounds other than silica or silica-containing material by reduction of silicon halides or halosilanes with a metal or a metallic alloy as the only reducing agents
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B33/00Silicon; Compounds thereof
    • C01B33/08Compounds containing halogen

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Silicon Compounds (AREA)

Abstract

Silicon halides are purified by contacting the halide in the vapour state with silicon at 850 DEG C. to 925 DEG C. The silicon should be as pure as possible, and the halide preferably remains in contact with the silicon for 0.1 to 10 seconds. The silicon halide may be prepurified by passing the vapour through a bed of fused silica rings at about 1000 DEG C., condensing the vapour, adding water, preferably 0.01 to 10% mols, allowing the mixture to stand, distilling it, and again vaporizing the halide prior to passing it over the silicon by dropping it on to fused silica chips maintained at 600-700 DEG C. All apparatus is preferably constructed of fused silica with welded joints, Silicon halides referred to include disilicon hexachloride, silicon tetrabromide, silicon tetraiodide, and especially silicon tetrachloride. The silicon halide thus purified may be converted to elemental silicon by reducing it with elemental zinc or cadmium in the vapour state. The zinc or cadmium vapour is preferably purified prior to the reduction by passing it through a bed of heated silicon at 800-1100 DEG C. in a similar fashion to that employed for purifying the halide. Preferably the reactants are passed p directly from the purifying steps to an elongated reactor, preferably maintained at a temperature above the boiling points of the reactants and by-products, and below the melting point of the silicon, for example about 950 or 1000 DEG C. A slight excess of the halide may be maintained. Crystalline silicon is deposited, and the by-product metal halide vapours and excess silicon halide vapours are removed and recovered. When the reactor is full of silicon the flow of metal vapour is stopped and the flow of halide continued for some time. The flow of halide is then stopped and the silicon product is then cooled with pinging by an inert gas, for example nitrogen.ALSO:Zinc or cadmium of high purity may be obtained by contacting the metal vapour with silicon at 800-1100 DEG C., preferably for a period of 0.1 to 10 seconds. The silicon should be as pure as possible. The thus purified metal vapour is used for the reduction of purified silicon halides to give pure silicon (see Group III).
GB2223557A 1957-07-12 1957-07-12 Improvements in or relating to the preparation of elemental silicon Expired GB867871A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB2223557A GB867871A (en) 1957-07-12 1957-07-12 Improvements in or relating to the preparation of elemental silicon

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB2223557A GB867871A (en) 1957-07-12 1957-07-12 Improvements in or relating to the preparation of elemental silicon

Publications (1)

Publication Number Publication Date
GB867871A true GB867871A (en) 1961-05-10

Family

ID=10176105

Family Applications (1)

Application Number Title Priority Date Filing Date
GB2223557A Expired GB867871A (en) 1957-07-12 1957-07-12 Improvements in or relating to the preparation of elemental silicon

Country Status (1)

Country Link
GB (1) GB867871A (en)

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