WO2012050341A3 - Fluidized bed reactor for preparing particulate polycrystalline silicon, and preparation method of polycrystalline silicon using same - Google Patents
Fluidized bed reactor for preparing particulate polycrystalline silicon, and preparation method of polycrystalline silicon using same Download PDFInfo
- Publication number
- WO2012050341A3 WO2012050341A3 PCT/KR2011/007522 KR2011007522W WO2012050341A3 WO 2012050341 A3 WO2012050341 A3 WO 2012050341A3 KR 2011007522 W KR2011007522 W KR 2011007522W WO 2012050341 A3 WO2012050341 A3 WO 2012050341A3
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- polycrystalline silicon
- fluidized bed
- bed reactor
- preparation
- same
- Prior art date
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
- C01B33/021—Preparation
- C01B33/027—Preparation by decomposition or reduction of gaseous or vaporised silicon compounds other than silica or silica-containing material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/1818—Feeding of the fluidising gas
- B01J8/1827—Feeding of the fluidising gas the fluidising gas being a reactant
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
- B01J8/38—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it
- B01J8/384—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only
- B01J8/386—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only internally, i.e. the particles rotate within the vessel
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
- B01J2208/00132—Tubes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
- B01J2208/0015—Plates; Cylinders
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00477—Controlling the temperature by thermal insulation means
- B01J2208/00495—Controlling the temperature by thermal insulation means using insulating materials or refractories
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00796—Details of the reactor or of the particulate material
- B01J2208/00893—Feeding means for the reactants
- B01J2208/00902—Nozzle-type feeding elements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00796—Details of the reactor or of the particulate material
- B01J2208/00991—Disengagement zone in fluidised-bed reactors
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/02—Apparatus characterised by their chemically-resistant properties
- B01J2219/0204—Apparatus characterised by their chemically-resistant properties comprising coatings on the surfaces in direct contact with the reactive components
- B01J2219/0218—Apparatus characterised by their chemically-resistant properties comprising coatings on the surfaces in direct contact with the reactive components of ceramic
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/02—Apparatus characterised by their chemically-resistant properties
- B01J2219/025—Apparatus characterised by their chemically-resistant properties characterised by the construction materials of the reactor vessel proper
- B01J2219/0277—Metal based
- B01J2219/0286—Steel
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Silicon Compounds (AREA)
Abstract
The present invention relates to a fluidized bed reactor for preparing particulate polycrystalline silicon, and a preparation method of polycrystalline silicon using the same. More specifically, the present invention provides a fluidized bed reactor for preparing particulate polycrystalline silicon in which a flowing gas is injected at a lower portion of a chamber and reaction is carried out at an upper portion of the chamber, and a preparation method of polycrystalline silicon using the same, wherein the fluidized bed reactor for preparing particulate polycrystalline silicon comprises: a closed chamber; a tubular heating device placed inside the chamber; a first supply pipe for supplying the flowing gas into the heating device, formed at the lower portion of the chamber; and a venturi for increasing the velocity of the flowing gas inside the heating device.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR10-2010-0099457 | 2010-10-12 | ||
KR1020100099457A KR101057101B1 (en) | 2010-10-12 | 2010-10-12 | Fluidized bed reactor for producing granular polycrystalline silicon and method of producing the same |
Publications (2)
Publication Number | Publication Date |
---|---|
WO2012050341A2 WO2012050341A2 (en) | 2012-04-19 |
WO2012050341A3 true WO2012050341A3 (en) | 2012-06-21 |
Family
ID=44933350
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/KR2011/007522 WO2012050341A2 (en) | 2010-10-12 | 2011-10-11 | Fluidized bed reactor for preparing particulate polycrystalline silicon, and preparation method of polycrystalline silicon using same |
Country Status (2)
Country | Link |
---|---|
KR (1) | KR101057101B1 (en) |
WO (1) | WO2012050341A2 (en) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103172067B (en) * | 2013-04-08 | 2014-09-24 | 无锡中彩科技有限公司 | Cold wall fluidized bed and application thereof |
KR101615307B1 (en) * | 2013-07-16 | 2016-04-25 | 웅진에너지 주식회사 | Polysilicon production apparatus |
WO2015008889A1 (en) * | 2013-07-16 | 2015-01-22 | 웅진에너지 주식회사 | Device and method for manufacturing polysilicon |
US9238211B1 (en) * | 2014-08-15 | 2016-01-19 | Rec Silicon Inc | Segmented silicon carbide liner |
DE102015224099A1 (en) * | 2015-12-02 | 2017-06-08 | Wacker Chemie Ag | Fluidized bed reactor and process for producing polycrystalline silicon granules |
EP3672910B1 (en) * | 2017-08-23 | 2021-07-21 | Wacker Chemie AG | Fluidized bed reactor for production of granular polycrystalline silicon |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5165908A (en) * | 1988-03-31 | 1992-11-24 | Advanced Silicon Materials, Inc. | Annular heated fluidized bed reactor |
US7029632B1 (en) * | 1999-10-06 | 2006-04-18 | Wacker-Chemie Gmbh | Radiation-heated fluidized-bed reactor |
KR20070080306A (en) * | 2006-02-07 | 2007-08-10 | 한국화학연구원 | High-pressure fluidized bed reactor for preparing granular polycrystalline silicon |
KR20080098322A (en) * | 2007-05-04 | 2008-11-07 | 와커 헤미 아게 | Process for the continuous production of polycrystalline high-purity silicon granules |
-
2010
- 2010-10-12 KR KR1020100099457A patent/KR101057101B1/en active IP Right Grant
-
2011
- 2011-10-11 WO PCT/KR2011/007522 patent/WO2012050341A2/en active Application Filing
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5165908A (en) * | 1988-03-31 | 1992-11-24 | Advanced Silicon Materials, Inc. | Annular heated fluidized bed reactor |
US7029632B1 (en) * | 1999-10-06 | 2006-04-18 | Wacker-Chemie Gmbh | Radiation-heated fluidized-bed reactor |
KR20070080306A (en) * | 2006-02-07 | 2007-08-10 | 한국화학연구원 | High-pressure fluidized bed reactor for preparing granular polycrystalline silicon |
KR20080098322A (en) * | 2007-05-04 | 2008-11-07 | 와커 헤미 아게 | Process for the continuous production of polycrystalline high-purity silicon granules |
Also Published As
Publication number | Publication date |
---|---|
WO2012050341A2 (en) | 2012-04-19 |
KR101057101B1 (en) | 2011-08-17 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO2012050341A3 (en) | Fluidized bed reactor for preparing particulate polycrystalline silicon, and preparation method of polycrystalline silicon using same | |
MY176065A (en) | Apparatus for producing trichlorosilane and method for producing trichlorosilane | |
IL202140A (en) | Method for the production of hydrogen from ammonia borane and its derivatives by homogeneous catalytic solvolysis reaction | |
EP1986956A4 (en) | Method for preparing granular polycrystalline silicon using fluidized bed reactor | |
GB2491994A (en) | Method and apparatus to release energy in a well | |
EP2409761A4 (en) | Catalyst for production of hydrogen and process for producing hydrogen using the catalyst, and catalyst for combustion of ammonia, process for producing the catalyst, and method for combustion of ammonia using the catalyst | |
WO2013016208A3 (en) | Reactant delivery system for ald/cvd processes | |
MX2013003233A (en) | Thermal fogging device using a liquid, and related method. | |
WO2008157519A3 (en) | Injector apparatus and method for production of nanostructures | |
EP1984297A4 (en) | High-pressure fluidized bed reactor for preparing granular polycrystalline silicon | |
MY180614A (en) | Apparatus and method for conversion of silicon tetrachloride to trichlorosilane | |
UA103890C2 (en) | Method and device for calciningg of gypsum under pressure | |
MY167549A (en) | A method for combined cleaning and plugging in a well and a flushing tool for flushing in a well | |
WO2012087628A3 (en) | Production of polycrystalline silicon by the thermal decomposition of dichlorosilane in a fluidized bed reactor | |
EP2479143A4 (en) | Reactor for producing polycrystalline silicon, system for producing polycrystalline silicon, and process for producing polycrystalline silicon | |
WO2012047035A3 (en) | Substrate processing device for supplying reaction gas through symmetry-type inlet and outlet | |
WO2009120862A3 (en) | Systems and methods for distributing gas in a chemical vapor deposition reactor | |
WO2013115711A3 (en) | Silicon carbide crystal growth in a cvd reactor using chlorinated chemistry | |
WO2010137858A3 (en) | Device for preparing bio-oil, system for preparing bio-oil and method for preparing bio-oil using the same | |
MY171935A (en) | Fluidized bed reactor and method of producing granular polysilicon | |
EP2694198A4 (en) | Method and arrangement for the supply of gas, or a mixture of gases, to a fluid | |
WO2013049314A3 (en) | Production of polycrystalline silicon by the thermal decomposition of silane in a fluidized bed reactor | |
UA104391C2 (en) | Method for production of trichlorosilane and silicon for use in production of trichlorosilane | |
MY170696A (en) | Process for operating a fluidized bed reactor | |
EP2433902A4 (en) | Method and device for producing combustible gas, heat energy, hydrogen and oxygen |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 11832728 Country of ref document: EP Kind code of ref document: A2 |
|
NENP | Non-entry into the national phase |
Ref country code: DE |
|
32PN | Ep: public notification in the ep bulletin as address of the adressee cannot be established |
Free format text: NOTING OF LOSS OF RIGHTS PURSUANT TO RULE 112(1) EPC (EPO FORM 1205 DATED 29-07-2013) |
|
122 | Ep: pct application non-entry in european phase |
Ref document number: 11832728 Country of ref document: EP Kind code of ref document: A2 |