AU2002215050A1 - Method for the production of high purity silicon - Google Patents
Method for the production of high purity siliconInfo
- Publication number
- AU2002215050A1 AU2002215050A1 AU2002215050A AU1505002A AU2002215050A1 AU 2002215050 A1 AU2002215050 A1 AU 2002215050A1 AU 2002215050 A AU2002215050 A AU 2002215050A AU 1505002 A AU1505002 A AU 1505002A AU 2002215050 A1 AU2002215050 A1 AU 2002215050A1
- Authority
- AU
- Australia
- Prior art keywords
- sub
- sih
- sihcl
- give
- feed gas
- 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.)
- Abandoned
Links
- 229910052710 silicon Inorganic materials 0.000 title abstract 4
- 239000010703 silicon Substances 0.000 title abstract 4
- 238000004519 manufacturing process Methods 0.000 title abstract 2
- 238000000034 method Methods 0.000 title abstract 2
- 238000006243 chemical reaction Methods 0.000 abstract 4
- SLLGVCUQYRMELA-UHFFFAOYSA-N chlorosilicon Chemical compound Cl[Si] SLLGVCUQYRMELA-UHFFFAOYSA-N 0.000 abstract 4
- 239000007789 gas Substances 0.000 abstract 4
- 238000007323 disproportionation reaction Methods 0.000 abstract 3
- ZDHXKXAHOVTTAH-UHFFFAOYSA-N trichlorosilane Chemical compound Cl[SiH](Cl)Cl ZDHXKXAHOVTTAH-UHFFFAOYSA-N 0.000 abstract 3
- 239000005052 trichlorosilane Substances 0.000 abstract 3
- 239000005046 Chlorosilane Substances 0.000 abstract 2
- 238000009835 boiling Methods 0.000 abstract 2
- KOPOQZFJUQMUML-UHFFFAOYSA-N chlorosilane Chemical class Cl[SiH3] KOPOQZFJUQMUML-UHFFFAOYSA-N 0.000 abstract 2
- 239000007787 solid Substances 0.000 abstract 2
- VXEGSRKPIUDPQT-UHFFFAOYSA-N 4-[4-(4-methoxyphenyl)piperazin-1-yl]aniline Chemical compound C1=CC(OC)=CC=C1N1CCN(C=2C=CC(N)=CC=2)CC1 VXEGSRKPIUDPQT-UHFFFAOYSA-N 0.000 abstract 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 abstract 1
- 230000003197 catalytic effect Effects 0.000 abstract 1
- 238000009833 condensation Methods 0.000 abstract 1
- 230000005494 condensation Effects 0.000 abstract 1
- 238000004821 distillation Methods 0.000 abstract 1
- 238000007700 distillative separation Methods 0.000 abstract 1
- IXCSERBJSXMMFS-UHFFFAOYSA-N hcl hcl Chemical compound Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 abstract 1
- 239000001257 hydrogen Substances 0.000 abstract 1
- 229910052739 hydrogen Inorganic materials 0.000 abstract 1
- 239000012535 impurity Substances 0.000 abstract 1
- 239000007788 liquid Substances 0.000 abstract 1
- 239000000203 mixture Substances 0.000 abstract 1
- 238000005201 scrubbing Methods 0.000 abstract 1
- 239000005049 silicon tetrachloride Substances 0.000 abstract 1
- 239000000725 suspension Substances 0.000 abstract 1
- 238000005979 thermal decomposition reaction Methods 0.000 abstract 1
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
- C01B33/029—Preparation by decomposition or reduction of gaseous or vaporised silicon compounds other than silica or silica-containing material by decomposition of monosilane
-
- 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
- C01B33/037—Purification
- C01B33/039—Purification by conversion of the silicon into a compound, optional purification of the compound, and reconversion into silicon
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01L—SEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
- H01L31/00—Semiconductor devices sensitive to infrared radiation, light, electromagnetic radiation of shorter wavelength or corpuscular radiation and specially adapted either for the conversion of the energy of such radiation into electrical energy or for the control of electrical energy by such radiation; Processes or apparatus specially adapted for the manufacture or treatment thereof or of parts thereof; Details thereof
- H01L31/18—Processes or apparatus specially adapted for the manufacture or treatment of these devices or of parts thereof
- H01L31/1804—Processes or apparatus specially adapted for the manufacture or treatment of these devices or of parts thereof comprising only elements of Group IV of the Periodic Table
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/50—Photovoltaic [PV] energy
- Y02E10/547—Monocrystalline silicon PV cells
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Condensed Matter Physics & Semiconductors (AREA)
- General Physics & Mathematics (AREA)
- Computer Hardware Design (AREA)
- Microelectronics & Electronic Packaging (AREA)
- Power Engineering (AREA)
- Electromagnetism (AREA)
- Physics & Mathematics (AREA)
- Manufacturing & Machinery (AREA)
- Silicon Compounds (AREA)
- Crystals, And After-Treatments Of Crystals (AREA)
Abstract
The invention relates to a method for the production of high purity silicon, characterized by the following steps: a) reaction of metallic silicon with silicon tetrachloride (SiCl<SUB>4</SUB>), hydrogen (H<SUB>2</SUB>) and hydrochloric acid (HCl) at a temperature of 500 to 800° C. and a pressure of 25 to 40 bar to give a trichlorosilane-containing (SiHCl<SUB>3</SUB>) feed gas stream, b) removal of impurities from the resultant trichlorosilane-containing feed gas stream by scrubbing with condensed chlorosilanes at a pressure of 25 to 40 bar and a temperature of 160 to 200° C. in a multi-stage distillation column, to give a purified trichlorosilane-containing feed gas stream and a solid-containing chlorosilane suspension and a distillative separation of the purified feed gas stream into a partial stream essentially comprising SiCl<SUB>4 </SUB>and a partial stream, essentially comprising SiHCl<SUB>3</SUB>, c) disproportionation of the SiHCl<SUB>3</SUB>-containing partial stream to give SiCl<SUB>4 </SUB>and SiH<SUB>4</SUB>, whereby the disproportionation is carried out in several reactive/distillative reaction zones, with a counter-current of vapour and liquid, on catalytic solids at a pressure of 500 mbar to 50 bar and SiHCl<SUB>3 </SUB>is introduced into a first reaction zone, the lower boiling SiH<SUB>4</SUB>-containing disproportionation product produced there undergoes an intermediate condensation in a temperature range of -25° C. to 50° C., the non-condensing SiH<SUB>4</SUB>-containing product mixture is fed to one or more further reactive/distillative reaction zones and the lower boiling product thus generated, containing a high proportion of SiH<SUB>4 </SUB>is completely or partially condensed in the head condenser and d) thermal decomposition of the SiH<SUB>4 </SUB>to give high purity silicon.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE10061682 | 2000-12-11 | ||
DE10061682A DE10061682A1 (en) | 2000-12-11 | 2000-12-11 | Process for the production of high-purity silicon |
PCT/EP2001/013507 WO2002048034A1 (en) | 2000-12-11 | 2001-11-21 | Method for the production of high purity silicon |
Publications (1)
Publication Number | Publication Date |
---|---|
AU2002215050A1 true AU2002215050A1 (en) | 2002-06-24 |
Family
ID=7666710
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
AU2002215050A Abandoned AU2002215050A1 (en) | 2000-12-11 | 2001-11-21 | Method for the production of high purity silicon |
Country Status (6)
Country | Link |
---|---|
US (1) | US6887448B2 (en) |
EP (1) | EP1341720B1 (en) |
AT (1) | ATE287853T1 (en) |
AU (1) | AU2002215050A1 (en) |
DE (2) | DE10061682A1 (en) |
WO (1) | WO2002048034A1 (en) |
Families Citing this family (48)
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DE10056194A1 (en) * | 2000-11-13 | 2002-05-29 | Solarworld Ag | Process for removing aluminum from chlorosilanes |
US7175685B1 (en) * | 2002-04-15 | 2007-02-13 | Gt Solar Incorporated | Dry conversion of high purity ultrafine silicon powder to densified pellet form for silicon melting applications |
US20070148034A1 (en) * | 2002-04-15 | 2007-06-28 | Gt Solar Incorporated | Dry conversion of high purity ultrafine silicon powder to densified pellet form for silicon melting applications |
US20060183958A1 (en) * | 2003-04-01 | 2006-08-17 | Breneman William C | Process for the treatment of waste metal chlorides |
DE102004010055A1 (en) * | 2004-03-02 | 2005-09-22 | Degussa Ag | Process for the production of silicon |
DE102004027563A1 (en) * | 2004-06-04 | 2005-12-22 | Joint Solar Silicon Gmbh & Co. Kg | Silicon and process for its production |
CN101143723B (en) | 2007-08-08 | 2010-09-01 | 徐州东南多晶硅材料研发有限公司 | Modified method and device for preparing trichlorosilane and multicrystal silicon |
US7754175B2 (en) * | 2007-08-29 | 2010-07-13 | Dynamic Engineering, Inc. | Silicon and catalyst material preparation in a process for producing trichlorosilane |
DE102008017304A1 (en) * | 2008-03-31 | 2009-10-01 | Schmid Silicon Technology Gmbh | Process and plant for the production of ultrapure silicon |
US7736614B2 (en) * | 2008-04-07 | 2010-06-15 | Lord Ltd., Lp | Process for removing aluminum and other metal chlorides from chlorosilanes |
US20100264362A1 (en) * | 2008-07-01 | 2010-10-21 | Yongchae Chee | Method of producing trichlorosilane (TCS) rich Chlorosilane product stably from a fluidized gas phase reactor (FBR) and the structure of the reactor |
US9067338B2 (en) * | 2008-08-04 | 2015-06-30 | Semlux Technologies, Inc. | Method to convert waste silicon to high purity silicon |
DE102008041974A1 (en) | 2008-09-10 | 2010-03-11 | Evonik Degussa Gmbh | Device, its use and a method for self-sufficient hydrogenation of chlorosilanes |
CN103787336B (en) * | 2008-09-16 | 2016-09-14 | 储晞 | The method producing high purity granular silicon |
US20100124525A1 (en) * | 2008-11-19 | 2010-05-20 | Kuyen Li | ZERO-HEAT-BURDEN FLUIDIZED BED REACTOR FOR HYDRO-CHLORINATION OF SiCl4 and M.G.-Si |
TW201113391A (en) * | 2009-03-19 | 2011-04-16 | Ae Polysilicon Corp | Silicide-coated metal surfaces and methods of utilizing same |
AU2010239352A1 (en) * | 2009-04-20 | 2011-11-10 | Ae Polysilicon Corporation | Processes and an apparatus for manufacturing high purity polysilicon |
JP2012523963A (en) * | 2009-04-20 | 2012-10-11 | エーイー ポリシリコン コーポレーション | Reactor with metal surface coated with silicide |
US8235305B2 (en) | 2009-04-20 | 2012-08-07 | Ae Polysilicon Corporation | Methods and system for cooling a reaction effluent gas |
KR20100117025A (en) * | 2009-04-23 | 2010-11-02 | 스미또모 가가꾸 가부시키가이샤 | Process for producing photoresist pattern |
US8298490B2 (en) | 2009-11-06 | 2012-10-30 | Gtat Corporation | Systems and methods of producing trichlorosilane |
KR101672796B1 (en) * | 2009-11-10 | 2016-11-07 | 주식회사 케이씨씨 | Method for producing high purity trichlorosilane for poly-silicon using chlorine gas or hydrogen chloride |
CN103025746A (en) | 2010-01-26 | 2013-04-03 | 道康宁公司 | Method of preparing an organohalosilane |
US8772525B2 (en) | 2010-05-28 | 2014-07-08 | Dow Corning Corporation | Method for preparing a diorganodihalosilane |
EP2576572A1 (en) | 2010-05-28 | 2013-04-10 | Dow Corning Corporation | Preparation of organohalosilanes |
US20110300050A1 (en) * | 2010-06-08 | 2011-12-08 | Memc Electronic Materials, Inc. | Trichlorosilane Vaporization System |
US8765090B2 (en) * | 2010-09-08 | 2014-07-01 | Dow Corning Corporation | Method for preparing a trihalosilane |
WO2012082686A1 (en) | 2010-12-17 | 2012-06-21 | Dow Corning Corporation | Method of making a trihalosilane |
RU2013122125A (en) | 2010-12-17 | 2015-01-27 | Дау Корнинг Корпорейшн | METHOD FOR PRODUCING DIORGANODIGALOGENILSILANE |
US8715597B2 (en) | 2010-12-20 | 2014-05-06 | Memc Electronic Materials, Inc. | Production of polycrystalline silicon in substantially closed-loop systems that involve disproportionation operations |
US8404205B2 (en) * | 2011-01-07 | 2013-03-26 | Mitsubishi Polycrystalline Silicon America Corporation (MIPSA) | Apparatus and method for producing polycrystalline silicon having a reduced amount of boron compounds by forming phosphorus-boron compounds |
RU2013125229A (en) | 2011-01-25 | 2015-03-10 | Дау Корнинг Корпорейшн | METHOD FOR PRODUCING DIORGANODIGALOGENILSILANE |
JP6040254B2 (en) | 2011-11-17 | 2016-12-07 | ダウ コーニング コーポレーションDow Corning Corporation | Method for preparing diorganodihalosilane |
CN102491337A (en) * | 2011-12-16 | 2012-06-13 | 大连理工常州研究院有限公司 | Method for preparing high-purity silicon powder through microwave plasma torch |
EP2639236A1 (en) | 2012-03-15 | 2013-09-18 | Dow Corning Corporation | Alternative methods for the synthesis of organosilicon compounds |
US10011493B2 (en) | 2012-04-27 | 2018-07-03 | Corner Star Limited | Methods for purifying halosilane-containing streams |
CN104736547A (en) | 2012-08-13 | 2015-06-24 | 道康宁公司 | Method of preparing an organohalosilane by reacting hydrogen, halosilane and organohalide in a two step process on a copper catalyst |
JP2015532683A (en) | 2012-08-30 | 2015-11-12 | ダウ コーニング コーポレーションDow Corning Corporation | Electrolytic process for silicides |
CN104583221B (en) | 2012-10-16 | 2018-05-01 | 道康宁公司 | The method for preparing halogenation sila Asia hydrocarbon |
US9352971B2 (en) | 2013-06-14 | 2016-05-31 | Rec Silicon Inc | Method and apparatus for production of silane and hydrohalosilanes |
JP6479794B2 (en) | 2013-11-12 | 2019-03-06 | ダウ シリコーンズ コーポレーション | Method for producing halosilane |
WO2016099690A1 (en) | 2014-12-18 | 2016-06-23 | Dow Corning Corporation | Method for producing aryl-functional silanes |
CN107108236A (en) * | 2014-12-18 | 2017-08-29 | 赫姆洛克半导体运营有限责任公司 | The method for hydrogenating halogenated silanes |
US11034585B2 (en) * | 2016-10-19 | 2021-06-15 | Tokuyama Corporation | Method for controlling concentration of solid content and method for producing trichlorosilane |
WO2019079879A1 (en) | 2017-10-27 | 2019-05-02 | Kevin Allan Dooley Inc. | A system and method for manufacturing high purity silicon |
CN110078080B (en) * | 2019-04-26 | 2022-09-02 | 天津科技大学 | Chlorosilane high-boiling-point substance recovery process combining slag slurry treatment and cracking reaction |
CN112456500A (en) * | 2021-01-29 | 2021-03-09 | 中国科学院过程工程研究所 | Preparation method of trichlorosilane |
KR102712596B1 (en) * | 2022-08-29 | 2024-09-30 | 오씨아이 주식회사 | Method for manufacturing silicon microparticles and silicon microparticles prepared by the same |
Family Cites Families (25)
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DE158322C (en) | ||||
US3012861A (en) * | 1960-01-15 | 1961-12-12 | Du Pont | Production of silicon |
BE784818A (en) * | 1971-06-14 | 1972-12-13 | Westinghouse Electric Corp | CALIBRATION OF THE MOVEMENT PROFILE OF THE POSITION OF A DRIVE BY MOTOR |
BE792542A (en) | 1971-12-11 | 1973-03-30 | Degussa | PROCESS FOR THE MANUFACTURE OF METAL-FREE CHLOROSILANES DURING THE CHLORINATION OR HYDROCHLORINATION OF FERROSILICIUM |
US3968199A (en) * | 1974-02-25 | 1976-07-06 | Union Carbide Corporation | Process for making silane |
DE2623290A1 (en) | 1976-05-25 | 1977-12-08 | Wacker Chemitronic | PROCESS FOR THE PRODUCTION OF TRICHLOROSILANE AND / OR SILICON TETRACHLORIDE |
US4117094A (en) * | 1977-06-13 | 1978-09-26 | Texas Instruments Incorporated | Process for silicon and trichlorosilane production |
US4676967A (en) * | 1978-08-23 | 1987-06-30 | Union Carbide Corporation | High purity silane and silicon production |
JPS5673617A (en) * | 1979-11-17 | 1981-06-18 | Osaka Titanium Seizo Kk | Manufacture of trichlorosilane |
DD158322A3 (en) * | 1980-02-19 | 1983-01-12 | Bernd Koehler | PROCESS FOR THE PREPARATION OF BORAROUS CHLOROSILANES |
US4519999A (en) * | 1980-03-31 | 1985-05-28 | Union Carbide Corporation | Waste treatment in silicon production operations |
US4340574A (en) * | 1980-08-28 | 1982-07-20 | Union Carbide Corporation | Process for the production of ultrahigh purity silane with recycle from separation columns |
DE3139705C2 (en) * | 1981-10-06 | 1983-11-10 | Wacker-Chemitronic Gesellschaft für Elektronik-Grundstoffe mbH, 8263 Burghausen | Process for processing the residual gases produced during silicon deposition and silicon tetrachloride conversion |
JPS58161915A (en) * | 1982-03-17 | 1983-09-26 | Shin Etsu Chem Co Ltd | Manufacture of trichlorosilane |
US4690810A (en) * | 1986-03-26 | 1987-09-01 | Union Carbide Corporation | Disposal process for contaminated chlorosilanes |
US4743344A (en) | 1986-03-26 | 1988-05-10 | Union Carbide Corporation | Treatment of wastes from high purity silicon process |
JPS63100014A (en) * | 1986-10-15 | 1988-05-02 | Mitsui Toatsu Chem Inc | Preparation of trichlorosilane |
JPH0788214B2 (en) * | 1986-10-15 | 1995-09-27 | 三井東圧化学株式会社 | Method for producing trichlorosilane |
JPS63100015A (en) * | 1986-10-15 | 1988-05-02 | Mitsui Toatsu Chem Inc | Preparation of trichlorosilane |
JP2613261B2 (en) * | 1988-06-09 | 1997-05-21 | 三井東圧化学株式会社 | Method for producing trichlorosilane |
JP2613260B2 (en) * | 1988-06-09 | 1997-05-21 | 三井東圧化学株式会社 | Method for producing trichlorosilane |
JP2613262B2 (en) * | 1988-06-10 | 1997-05-21 | 三井東圧化学株式会社 | Method for producing trichlorosilane |
DE4104422C2 (en) | 1991-02-14 | 2000-07-06 | Degussa | Process for the preparation of trichlorosilane from silicon tetrachloride |
US5798137A (en) * | 1995-06-07 | 1998-08-25 | Advanced Silicon Materials, Inc. | Method for silicon deposition |
US6368568B1 (en) * | 2000-02-18 | 2002-04-09 | Stephen M Lord | Method for improving the efficiency of a silicon purification process |
-
2000
- 2000-12-11 DE DE10061682A patent/DE10061682A1/en not_active Withdrawn
-
2001
- 2001-11-21 DE DE50105221T patent/DE50105221D1/en not_active Expired - Lifetime
- 2001-11-21 EP EP01983594A patent/EP1341720B1/en not_active Expired - Lifetime
- 2001-11-21 AT AT01983594T patent/ATE287853T1/en not_active IP Right Cessation
- 2001-11-21 AU AU2002215050A patent/AU2002215050A1/en not_active Abandoned
- 2001-11-21 US US10/450,125 patent/US6887448B2/en not_active Expired - Fee Related
- 2001-11-21 WO PCT/EP2001/013507 patent/WO2002048034A1/en not_active Application Discontinuation
Also Published As
Publication number | Publication date |
---|---|
WO2002048034A1 (en) | 2002-06-20 |
US20040047797A1 (en) | 2004-03-11 |
ATE287853T1 (en) | 2005-02-15 |
EP1341720A1 (en) | 2003-09-10 |
US6887448B2 (en) | 2005-05-03 |
DE10061682A1 (en) | 2002-07-04 |
EP1341720B1 (en) | 2005-01-26 |
DE50105221D1 (en) | 2005-03-03 |
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