JPS6465010A - Device for producing high-purity granular metallic silicon - Google Patents
Device for producing high-purity granular metallic siliconInfo
- Publication number
- JPS6465010A JPS6465010A JP22032887A JP22032887A JPS6465010A JP S6465010 A JPS6465010 A JP S6465010A JP 22032887 A JP22032887 A JP 22032887A JP 22032887 A JP22032887 A JP 22032887A JP S6465010 A JPS6465010 A JP S6465010A
- Authority
- JP
- Japan
- Prior art keywords
- vessel
- metallic silicon
- grains
- purity
- fluidized bed
- 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.)
- Pending
Links
- 229910052710 silicon Inorganic materials 0.000 title abstract 7
- 239000010703 silicon Substances 0.000 title abstract 7
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 abstract 6
- 239000007789 gas Substances 0.000 abstract 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 abstract 2
- 239000001257 hydrogen Substances 0.000 abstract 2
- 229910052739 hydrogen Inorganic materials 0.000 abstract 2
- 239000002184 metal Substances 0.000 abstract 1
Landscapes
- Silicon Compounds (AREA)
Abstract
PURPOSE:To continuously produce the title high-purity granular metallic silicon with low power consumption by providing a flow straightening device in a reaction vessel to form a fluidized bed, furnishing a heater on the outside of the vessel, and making the vessel and the device from a metallic silicon plate. CONSTITUTION:The flow straightening device 3 made from a high-purity metallic silicon plate is provided in the vicinity of the bottom of the reaction vessel 1 made from a high-purity metallic silicon plate, and the fluidized bed 2 of the high-purity metallic silicon grains packed in the vessel 1 is formed. The heaters 9a and 9b are provided at the upper and lower parts on the outside of the vessel 1 to adjust the internal temp. of the vessel 1 to a temp. appropriate for the reaction. The raw gas and hydrogen are blown into the fluidized bed 2 heated by the heaters 9a and 9b from the lower part, and the silicon in the raw gas is reduced and deposited on the surface of the high-purity metal grains. The grains with the increased diameter are moved to the lower part, and classified by the gas sent from a classifying gaseous hydrogen supply pipe 5. The small-diameter grains are returned to the fluidized bed 2. Only the grains having a sufficiently large diameter are discharged from a discharge pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP22032887A JPS6465010A (en) | 1987-09-04 | 1987-09-04 | Device for producing high-purity granular metallic silicon |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP22032887A JPS6465010A (en) | 1987-09-04 | 1987-09-04 | Device for producing high-purity granular metallic silicon |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS6465010A true JPS6465010A (en) | 1989-03-10 |
Family
ID=16749421
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP22032887A Pending JPS6465010A (en) | 1987-09-04 | 1987-09-04 | Device for producing high-purity granular metallic silicon |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6465010A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2002094714A1 (en) * | 2001-05-22 | 2002-11-28 | Solarworld Aktiengesellschaft | Method for producing highly pure, granular silicon in a fluidised bed |
| JP2003002628A (en) * | 2001-06-21 | 2003-01-08 | Tokuyama Corp | Silicon manufacturing apparatus and manufacturing method |
| US6704592B1 (en) | 2000-06-02 | 2004-03-09 | Medrad, Inc. | Communication systems for use with magnetic resonance imaging systems |
| WO2006007082A3 (en) * | 2004-06-18 | 2006-09-08 | Memc Electronic Materials | Systems and methods for manufacturing granular material, and for measuring and reducing dust in granular material |
| JP2009502704A (en) * | 2005-07-19 | 2009-01-29 | アールイーシー シリコン インコーポレイテッド | Silicon jet fluidized bed |
-
1987
- 1987-09-04 JP JP22032887A patent/JPS6465010A/en active Pending
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6704592B1 (en) | 2000-06-02 | 2004-03-09 | Medrad, Inc. | Communication systems for use with magnetic resonance imaging systems |
| WO2002094714A1 (en) * | 2001-05-22 | 2002-11-28 | Solarworld Aktiengesellschaft | Method for producing highly pure, granular silicon in a fluidised bed |
| US7553466B2 (en) | 2001-05-22 | 2009-06-30 | Solarworld Aktiengesellschaft | Method for producing highly pure, granular silicon in a fluidised bed |
| JP2003002628A (en) * | 2001-06-21 | 2003-01-08 | Tokuyama Corp | Silicon manufacturing apparatus and manufacturing method |
| WO2006007082A3 (en) * | 2004-06-18 | 2006-09-08 | Memc Electronic Materials | Systems and methods for manufacturing granular material, and for measuring and reducing dust in granular material |
| US7291222B2 (en) | 2004-06-18 | 2007-11-06 | Memc Electronic Materials, Inc. | Systems and methods for measuring and reducing dust in granular material |
| JP2009502704A (en) * | 2005-07-19 | 2009-01-29 | アールイーシー シリコン インコーポレイテッド | Silicon jet fluidized bed |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US2477454A (en) | Process of reducing ferric oxide to ferrosoferric oxide | |
| CN1048746C (en) | Decomposition reactor | |
| US4046548A (en) | Apparatus for producing spherical particles | |
| JPS6415334A (en) | Production of metal from metal halide | |
| US4894081A (en) | Spherulizing furnace | |
| JPS6465010A (en) | Device for producing high-purity granular metallic silicon | |
| KR970029900A (en) | Cyclone and Fluidized Bed Reactor with the Same | |
| EP0246191A3 (en) | Teatment of solids in a fluidized bed burner | |
| SU1634141A3 (en) | Process and shaft furnace for direct gas reduction of granulated iron ore | |
| US2516974A (en) | Method and apparatus for gasifying carbonaceous material | |
| CN2487738Y (en) | Partition board type internal circulation fluidized bed gasification furnace | |
| US5006062A (en) | Treatment of solids in fluidized bed burner | |
| GB1584175A (en) | Apparatus for producing spherical particles | |
| CN105819449B (en) | Silane moving-burden bed reactor and the method that granular polycrystalline silicon is produced using the reactor | |
| CA2084979A1 (en) | Prevention of blockage of charge feed tube in smelting furnace | |
| RU2006114669A (en) | DEVICE AND METHOD FOR PROCESSING GASES BY THE MOBILE LAYER OF MATERIAL FROM MACROPARTICLES | |
| CN1110680C (en) | Furnace for expanding perlite | |
| CA2052140A1 (en) | Fluidized bed apparatus for chemically treating workpieces | |
| JPS5941772B2 (en) | Ultrafine powder synthesis furnace | |
| CN1029371C (en) | Making method of active lime powder agent for injection metallurgy | |
| RU99104692A (en) | METHOD FOR PRODUCING MONOSILANE FROM SILICON TETRACHLORIDE | |
| CN206466974U (en) | A kind of copper powder fluid bed | |
| CN2170952Y (en) | Cross pot type reducing furnace for magnesium smelting by hot reducing method | |
| JPS56169769A (en) | Carbonitriding method | |
| JPH02279512A (en) | Production of high-purity polycrystal silicon |