GB980173A - Process for the manufacture of very pure silicon - Google Patents
Process for the manufacture of very pure siliconInfo
- Publication number
- GB980173A GB980173A GB601761A GB601761A GB980173A GB 980173 A GB980173 A GB 980173A GB 601761 A GB601761 A GB 601761A GB 601761 A GB601761 A GB 601761A GB 980173 A GB980173 A GB 980173A
- Authority
- GB
- United Kingdom
- Prior art keywords
- gases
- stage
- sicl4
- halogeno
- decomposition
- 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
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/02—Silicon
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Silicon Compounds (AREA)
Abstract
Very pure Si is manufactured by reduction decomposition of a halogeno-silano with H2 at 800-1400 DEG C. in contact with directly or indirectly heated carrier bodies; the reaction gases from the decomposition zone are passed through a heated static or fluidized bed of particulate Al which reacts with the HCl to form AlCl3 which is precipitated by cooling the gases, the residual gases after addition of fresh halogeno-silane, and if desired H2, are returned to the decomposition zone. The halogeno-silane may be SiCl4 or mono-, di- or tri-chlorosilane. In stage 1, Fig. 1, Si is produced by reductive decomposition at e.g. superatmospheric pressure. In stage 2 the reaction vessel is e.g. of steel or quartz and the Al bed is at 50-500 DEG C., preferably below 300 DEG C. for SiCl4 and above 300 DEG C. for SiHCl3. <PICT:0980173/C1/1> In stage 3 the vessel is at 20-80 DEG C., contains members of large surface area, e.g. metal plates, wire netting, fibres or finely divided filter material, and may be divided into 2 parts through which the gases flow successively, in the first part the greater part of the AlCl3 is precipitated and the second part, in which the gases are clean, contains very fine filter material, e.g. quartz wool. In an optional stage 4, the SiCl4 is condensed, e.g. fractionally, and then returned to storage vessel 9 or in Fig. 2 (not shown) to the gases resulting from the reaction of SiHCl3 and H2. The Si may be repeatedly zone-refined to give a high specific resistance and can be used as a semi-conductor.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEW27269A DE1105397B (en) | 1960-02-18 | 1960-02-18 | Process for the production of high purity silicon |
Publications (1)
Publication Number | Publication Date |
---|---|
GB980173A true GB980173A (en) | 1965-01-13 |
Family
ID=7598593
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB601761A Expired GB980173A (en) | 1960-02-18 | 1961-02-17 | Process for the manufacture of very pure silicon |
Country Status (3)
Country | Link |
---|---|
CH (1) | CH426749A (en) |
DE (1) | DE1105397B (en) |
GB (1) | GB980173A (en) |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1053478B (en) * | 1956-12-24 | 1959-03-26 | Texas Instruments Inc | Process for converting silicon tetrachloride into highly purified silicon |
-
1960
- 1960-02-18 DE DEW27269A patent/DE1105397B/en active Pending
-
1961
- 1961-02-07 CH CH144061A patent/CH426749A/en unknown
- 1961-02-17 GB GB601761A patent/GB980173A/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
CH426749A (en) | 1966-12-31 |
DE1105397B (en) | 1961-04-27 |
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