SA515360365B1 - Method and apparatus to reduce contamination of particles in a fluidized bed reactor - Google Patents

Method and apparatus to reduce contamination of particles in a fluidized bed reactor Download PDF

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SA515360365B1
SA515360365B1 SA515360365A SA515360365A SA515360365B1 SA 515360365 B1 SA515360365 B1 SA 515360365B1 SA 515360365 A SA515360365 A SA 515360365A SA 515360365 A SA515360365 A SA 515360365A SA 515360365 B1 SA515360365 B1 SA 515360365B1
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Saudi Arabia
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fluidized bed
bed reactor
protective layer
reactor
silicon
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SA515360365A
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Arabic (ar)
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مايكل، في سبانجلر،
ماتثيو، جيه ميلر،
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آر إي سي سيليكون إنك
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Priority claimed from US13/670,200 external-priority patent/US9587993B2/en
Priority claimed from US13/939,067 external-priority patent/US9212421B2/en
Application filed by آر إي سي سيليكون إنك filed Critical آر إي سي سيليكون إنك
Publication of SA515360365B1 publication Critical patent/SA515360365B1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/02Apparatus characterised by being constructed of material selected for its chemically-resistant properties
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/1809Controlling processes
    • 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
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/22Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the deposition of inorganic material, other than metallic material
    • C23C16/24Deposition of silicon only
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/44Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
    • C23C16/4401Means for minimising impurities, e.g. dust, moisture or residual gas, in the reaction chamber
    • C23C16/4404Coatings or surface treatment on the inside of the reaction chamber or on parts thereof
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/44Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
    • C23C16/442Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating using fluidised bed process
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049Controlling or regulating processes
    • B01J2219/00245Avoiding undesirable reactions or side-effects
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/02Apparatus characterised by their chemically-resistant properties
    • B01J2219/0204Apparatus characterised by their chemically-resistant properties comprising coatings on the surfaces in direct contact with the reactive components
    • B01J2219/0236Metal based

Abstract

METHOD AND APPARATUS TO REDUCE CONTAMINATION OF PARTICLES IN A FLUIDIZED BED REACTOR ABSTRACT A method and fluidized bed reactor for reducing or eliminating contamination of silicon-coated particles are disclosed. The metal surface of one or more fluidized bed reactor components is at least partially coated with a hard protective layer comprising a material having an ultimate tensile strength of at least 700 MPa at 650 °C. Fig 1

Claims (1)

-١١- ‏عناصر الحمابة‎ sificon-coated ‏أو إزالة تلوث الجزيئات المغلفة بالسيليكون‎ reducing ‏لتقليل‎ method ‏طريقة‎ -١ fluidized bed ‏في مفاعل الطبقة المُميعة‎ surface ‏مع السطح‎ contact ‏بسبب الإتصال‎ particles ‏الطريقة متضمنة:‎ 207 fluidized ‏مكون مفاعل الطبقة المُميعة‎ fluidized bed reactor ‏توفير؛ في مفاعل الطبقة المُميعة‎ silicon-coated ‏مواجه الجزيئات المغلفة بالسيليكون‎ surface ‏له سطح‎ bed reactor component 8 ‏يضم معدن‎ surface ‏1:0:280ء السطح‎ bed reactor ‏أثنا ء تشغيل مفاعل الطبقة المُميعة‎ particles ‏مشتمل على‎ protective layer ‏بطبقة واقية‎ partially coated ‏يكون مغلف على الأقل جزئيا‎ metal ‏ميجا باسكال عند‎ 7٠١ ‏على الأقل‎ ultimate tensile strength ‏لها قوة شد قصوي‎ material ‏مادة‎ ‏تكون‎ protective layer ‏تم؛ وفيه الطبقة الواقية‎ (0 > (Ni 96٠١ > W 70٠١ > Cr %Yo-Yo ‏مشتملة على‎ cobalt ‏أساسها كوبلت‎ alloy ‏سبيكة‎ ٠ > ‏ق > ...17 0ه‎ %Y > Mn %V,0 > 9١ > Si %Y > Fe %Y > Mo 75 ‏أو‎ cobalt ‏كوبلت‎ %Vo-Y.,0 ‏58و‎ 5 «Co 76٠١-١7 «Cr %Yo—0 Mo %Y¥ —¢ ‏على‎ dla da nickel ‏أساسها النيكل‎ alloy ‏سبيكة‎ ‎«© % +.) > Cu ‏مق‎ > Si%Y) > Mn 96١ > Al %Y > Fe %Y > (Ti 9636 > ‏و‎ tnickel ‏نيكل‎ 9681-77, B ‏م > لاس > د16‎ silicon- ‏لصنع جزيئات مغلفة بالسيليكون‎ fluidized bed reactor ‏تشغيل مفاعل الطبقة المُميعة‎ .coated particles surface ‏من المطح‎ 70955 coated ‏وفقا للعنصر ١؛ حيث يتم تغليف‎ method ‏الطريقة‎ -" .protective layer ‏بالطيبقة الواقية‎ ٠ thermal | ‏معامل حراري للتمدد‎ metal ‏وفقا للعنصر ١؛ حيث للمعدن‎ method ‏الطريقة‎ — ‏لها معامل حراري للتمدد‎ protective layer ‏وطبقة واقية‎ «TCE -١ «coefficient of expansion TCE =) ‏حيث يكون الفرق بين 7- 1025و‎ (TCE —V «thermal coefficient of expansion .7٠ > ‏هو‎ Yo ‏امه‎-11- sificon-coated elements or reducing contamination of silicon-coated particles to reduce method Method 1 fluidized bed in fluidized bed reactor surface with surface contact due to contact particles method included : 207 fluidized fluidized bed reactor component supplied; In a silicon-coated fluidized bed reactor facing the silicon-coated surface has a surface bed reactor component 8 comprising a metal surface 1:0:280 – the surface bed reactor during operation of the fluidized bed reactor contains particles protective layer with protective layer, partially coated, at least partially coated, metal MPa, at least 701, ultimate tensile strength material, protective layer; In which the protective layer (0 > (Ni 9601 > W 7001 > Cr %Yo-Yo) containing cobalt based alloy alloy 0 > s > ...17 0e %Y > Mn %V, 0 > 91 > Si %Y > Fe %Y > Mo 75 or cobalt %Vo-Y.,0 cobalt 58, 5 “Co 7601-17 “Cr %Yo—0 Mo %Y¥ —¢ dla da nickel alloy «© % +.) > Cu M > Si%Y) > Mn 961 > Al %Y > Fe %Y > (Ti 9636 > tnickel Nickel 9681-77, B M > Las > D16 silicon- for making fluidized bed reactor coated particles surface 70955 coated according to item 1; method method - “.protective layer in the protective layer 0 thermal | thermal expansion coefficient metal according to item 1; where the metal method method — has a thermal expansion coefficient protective layer and a protective layer “TCE -1 “coefficient of expansion TCE =) where the difference is between 1025-7 and (TCE —V “thermal coefficient of expansion .70 > Yo is its mother) -١ ‏له‎ intermediate coating ‏حيث يتم وضع غلاف متوسط‎ oF ‏وفقا للعنصر‎ method ‏؛- الطريقة‎ 1086-7 108-7١ ‏بين‎ 1208-١ «thermal coefficient of expansion ‏معامل حراري للتمدد‎ .protective layer ‏والطبقة الواقية‎ metal ‏بين المعدن‎ ‏أدنى متوسط منمك‎ protective layer ‏وفقا للعنصر ١؛ حيث للطبقة الواقية‎ method ‏الطريقة‎ -#« © ‏د مم.‎ ١ ‏سلمك يختلف عبر‎ protective layer ‏وفقا للعنصر ©؛ حيث للطبقة الواقية‎ method ‏الطريقة‎ -7 surface ‏و/أو على طول طول السطح‎ width ‏الإتساع‎ ‎Ye ‏الطبقة‎ Jolie ‏من مكون‎ portion ‏وفقا للعنصر ١؛ حيث يتم إنشاء جزء‎ method ‏الطريقة‎ —V ‏كاملا من مادة لها إلى حد كبير نفس التركيبة‎ fluidized bed reactor component ‏المميعة‎1- It has an intermediate coating in which an intermediate coating of oF is placed according to the method method 1086-7 108-71 between 1208-1 “thermal coefficient of expansion . and the protective layer metal between the metal is the lowest medium patterned protective layer according to item 1; where for the protective layer method -#« © d mm. 1 Your ladder varies across the protective layer according to the element ©; where for the protective layer method -7 surface and/or along the surface width width Ye layer Jolie of portion component according to item 1; where the entire method —V part is constructed of material having substantially the same composition as the fluidized bed reactor component ‎.protective layer ‏للطبقة الواقية‎ chemical composition ‏الكيميائية‎ ‎fluidized bed reactor ‏وفقا للعنصر )¢ حيث مُكون مفاعل الطبقة المُميعة‎ method ‏الطريقة‎ =A Vo fluidization gas inlet ‏ممتاععزمت أنبوب مدخل غاز التمييع‎ nozzle ‏الحقن‎ dass ‏هو‎ component product withdrawal ‏8660؛ أنبوب خروج استعادة المنتج‎ inlet tube ‏مدخل البذور‎ sail tube sample nozzle ‏فوهة العينة‎ (probe assembly ‏تركيب المسبار‎ liner ‏البطانة‎ coutlet tube cnternal heater ‏سخان داخلي‎ cthermocouple ‏مزدوج حراري‎ pressure nozzle ‏فوهة الضغط‎ .bubble breaker ‏أو قاطع النفاخة‎ ٠ ‏لإنتاج السيليكون متعدد البلورات‎ fluidized bed reactor unit ‏وحدة مفاعل الطبقة المُميعة‎ -4 ‏مشتملة على:‎ unit ‏الوحدة‎ «polycrystalline silicon ‏و‎ «reactor chamber ‏يحدد غرفة للمفاعل‎ reactor ‏مفاعل‎ ‏مواجه غرفة المفاعل‎ surface ‏لها سطح‎ reactor components ‏واحد أو أكثر من مكونات المفاعل‎ Yo ‏والذي يكون مغطى بشكل جزئي على‎ metal ‏يضم معدن‎ surface ‏السطح‎ reactor chamber ‏على الأقل‎ ultimate tensile strength ‏لها قوة شد قصوي‎ protective layer ‏الأقل بطبقة واقية‎ ‏تكون‎ protective layer ‏ميجا باسكال عند 156 #م؛ وفيه الطبقة الواقية‎ ٠ ‏امه‎.protective layer for the chemical composition fluidized bed reactor according to the element ¢ where the fluidized bed reactor component method =A Vo fluidization gas inlet fluidized bed reactor nozzle dass is component product withdrawal 8660; Product recovery exit tube inlet tube seed inlet sail tube sample nozzle probe assembly liner coutlet tube cnternal heater internal heater cthermocouple thermocouple pressure nozzle pressure nozzle . bubble breaker or blow breaker 0 for the production of polycrystalline silicon fluidized bed reactor unit fluidized bed reactor unit 4- comprising: unit “polycrystalline silicon” and “reactor chamber” specifying a room for the reactor Reactor facing the reactor chamber surface having a surface reactor components one or more of the reactor components Yo which is partially covered on metal including metal surface surface reactor chamber at least ultimate tensile strength It has a maximum tensile strength, the protective layer, the least with a protective layer, which is MPa at 156 #m, and in which the protective layer is 0 mA > (Ni %Y + > W 7٠١ < «Cr %Yo-Yo ‏مشملة على‎ cobalt ‏أساسها كوبلت‎ alloy ‏سبيكة‎ ‎> P 17... > ‏ق‎ 7١ > Mn ١,0 ‏ح<‎ C %Y > Si %Y > Fe %Y > Mo 75 ‏أو‎ cobalt ‏كربلت‎ 679-7١ ‏و‎ 58 65 «Co 7١٠١-١ «Cr %Yo—-2 ‏ماك‎ %Y.—¢ le ‏مشتملة‎ nickel ¢ | ‏أساسها أ أنيك‎ alloy au or 0 % NY > ‏م17 م‎ > Si %Y > Mn 7١ > (Al %Y > (Fe %Y > (Ti %Y,0 > ° ‘nickel ‏حك96/8 نيكل‎ Y,¢ ‏و‎ 964 oY > Ir % + ,١ << silicon- ‏لصنع جزيئات مغلفة بالسيليكون‎ fluidized bed reactor ‏تشغيل مفاعل الطبقة المُميعة‎ ..coated particles ‎-٠١ Vo‏ وحدة مفاعل الطبقة المُميعة ‎fluidized bed reactor unit‏ للعنصر 8( حيث للمعدن ‎metal‏ معامل تمدد حراري ‎first thermal coefficient of expansion (1- TCE) Js‏ وللطبقة الواقية ‎protective layer‏ معامل تمدد حراري ‎second thermal coefficient of (2- TCE) SU‏ ‎expansion‏ الذي يختلف عن ‎1085-١‏ بج ‎SYS‏ ‎-١١‏ وحدة مفاعل الطبقة ‎fluidized bed reactor unit Amped)‏ وفقا للعنصر ‎١٠١‏ حيث يتضمن مُكون المفاعل أيضا غلاف متوسط ‎intermediate coating‏ له معامل حراري للتمدد ‎thermal‏ ‎«TVE-3 «coefficient of expansion‏ بين )= ‎TCE‏ و 108-7؛ حيث تقع الطبقة المتوسطة بين المعدن ‎metal‏ والطبقة الواقية ‎.protective layer‏ ‎-١" ٠‏ وحدة مفاعل الطبقة المُميعة ‎fluidized bed reactor unit‏ وفقا للعنصر 9؛ حيث للطبقة الواقية ‎protective layer‏ متوسط ‎average thickness Gli‏ من )+ مم إلى ‎١‏ مم. ‎-٠‏ وحدة مفاعل الطبقة ‎The fluidized bed reactor unit Amped)‏ وفقا للعنصر ‎VY‏ حيث للطبقة الواقية ‎protective layer‏ ملمك ‎thickness‏ يختلف عبر الإتساع ‎width‏ و/أو على طول> (Ni %Y + > W 701 < “Cr %Yo-Yo including cobalt alloy > P 17... > S 71 > Mn 1,0 H< C %Y > Si %Y > Fe %Y > Mo 75 or cobalt carbonate 679-71 and 58 65 «Co 7101-1 »Cr %Yo—-2 Mac %Y.—¢ le including nickel ¢ | based on annic alloy au or 0 % NY > M17 M > Si %Y > Mn 71 > (Al %Y > (Fe %Y > (Ti %Y,0 > ° 'nickel Silicon 96/8 nickel Y, ¢ and 964 oY > Ir % + 1, << silicon- to make fluidized bed reactor fluidized bed reactor operation of the fluidized bed reactor ..coated particles -01 Vo reactor unit The fluidized bed reactor unit of element 8 (where metal has a first thermal coefficient of expansion (1- TCE) Js and the protective layer has a second thermal coefficient of (2- TCE) ) SU expansion which differs from 1085-1B SYS -11 fluidized bed reactor unit Amped) according to item 101 where the reactor component also includes an intermediate coating for it thermal coefficient of expansion ‎«TVE-3« coefficient of expan sion between ) = TCE and 108-7; Where the intermediate layer is located between the metal and the protective layer. (+ mm to 1 mm. -0 The fluidized bed reactor unit Amped) according to element VY where the protective layer has a thickness that varies across width and/or Along ‎.surface ‏طول السطح‎ Yo ‏رمه ym ‏وفقا للعنصر 9؛ حيث يتم إنشاء‎ fluidized bed reactor unit ‏مفاعل الطبقة المُميعةٌ‎ sang - ٠4 ‏لها إلى حد كبير‎ material ‏بالتمام من مادة‎ reactor component ‏من مكون مفاعل‎ portion ‏جزء‎.surface The length of the surface Yo ram ym according to item 9; where the fluidized bed reactor unit sang - 04 fluidized bed reactor is largely constructed entirely of material reactor component of a portion reactor component ‎.protective layer ‏للطبقة الواقية‎ chemical ‏نفس التركيبة الكيميائية‎ 14-9 ‏وفقا لأي من العناصر‎ fluidized bed reactor unit ‏وحدة مفاعل الطبقة المميعة‎ -١# © ‏سبيكة‎ ccobalt-based alloy ‏سبيكة اساسها كوبلت‎ protective layer ‏حيث تتضمن الطبقة الواقية‎ ‏أو أي تركيبة متحدة منهم.‎ «nickel-based alloy ‏أساسها تيكل‎ granulate polycrystalline ‏لإنتاج جزيئات سيليكون متعددة البلورات حبيبية‎ process ‏عملية‎ =) siicon-containing ‏حيث تتضمن العملية تدفق الغاز المحتوي على السيليكون‎ silicon particles ٠ seed particle ‏المحتوي على جزئ بذور‎ fluidized bed reactor ‏خلال مفاعل الطبقة المُميعة‎ gas ‏لتؤثر‎ fluidized bed reactor ‏المُحددة بمفاعل الطبقة المُميعة‎ reactor chamber ‏في غرفة المفاعل‎ effect pyrolysis of the silicon-containing ‏على التحلل الحراري للغاز المحتوي على السيليكون‎ ‏على‎ deposition of polycrystalline silicon ‏وترسيب طبقة السيليكون متعدد البلوراتعتنيها‎ gas polycrystalline ‏لتكوين جزئ مغلف بالسيليكون متعدد البلورات‎ 60 particle ‏جزئ البذور‎ VO ‏واحد أو‎ fluidized bed reactor ‏ل02180©-511600» حيث يتضمن مفاعل الطبقة المُميعة‎ particle ‏مواجه لغرفة المفاعل‎ surface ‏التي لها سطح‎ reactor components ‏من مكونات المفاعل‎ as surface ‏يكون السطح‎ cduring reactor operation ‏أثنا ء تشغيل المفاعل‎ reactor chamber ‏بطبقة واقية‎ at least partially coated ‏جزئيا‎ JAY) ‏المُغلف على‎ metal ‏متضمن للمعدن‎ ‏ميجا باسكال عند‎ 7٠٠9 ‏على الأقل‎ ultimate tensile strength ‏تملك 353 شد‎ protective layer ٠٠ ‏تكون‎ protective layer ‏وفيه الطبقة الواقية‎ (2° (0 > (Ni %Y + > W 7٠١ > «Cr %Yo-Yo ‏مشملة على‎ cobalt ‏أساسها كوبلت‎ alloy ‏سبيكة‎ ‎> ‏ق > ...17 0ه‎ 7١ > Mn 7١,٠ > 9١ > Si %Y > Fe %Y > Mo 75 ‏أو‎ cobalt ‏كوبلت‎ %Vo-Y.,0 ‏58و‎ 5 «Co %\o—Y «Cr %Yo—0 Mo ؟؟؟١-؛ ‏مشتملة على‎ nickel ‏أساسها النيكل‎ alloy ‏سبيكة‎ YO «© % +.) > Cu ‏مق‎ > Si%Y) > Mn 96١ > Al %Y > Fe %Y > (Ti 9636 > ‏و‎ tnickel ‏نيكل‎ %AR=YY,€ ‏ل و‎ 96,1 > Zr %or,) > COAY.protective layer For the protective layer chemical Same chemical composition 14-9 According to any of the elements fluidized bed reactor unit fluidized bed reactor unit -1# © ccobalt-based alloy protective cobalt-based alloy layer where it includes the protective layer or any combined combination thereof. “nickel-based alloy granulate polycrystalline to produce granular polycrystalline silicon particles process =) siicon-containing where the process includes the flow of the containing gas On silicon particles 0 seed particle containing a fluidized bed reactor seed particle through the gas fluidized bed reactor to affect the fluidized bed reactor reactor chamber effect pyrolysis of the silicon-containing On thermal decomposition of silicon-containing gas On deposition of polycrystalline silicon and deposition of a layer of polycrystalline silicon gas polycrystalline to form a polycrystalline silicon-encapsulated molecule 60 particle seed molecule VO one or fluidized bed reactor for © 02180 - 511600 » where the fluidized bed reactor includes a particle facing the reactor chamber surface that has a surface reactor components as surface cduring reactor operation reactor chamber reactor chamber with a protective layer at least partially coated (JAY) coated on metal containing metal MPa at least 7009 ultimate tensile strength has 353 tensile protective layer 00 to be protective layer and in it the protective layer (2° (0 > (Ni %Y + > W 701 > “Cr %Yo-Yo including cobalt based alloy > s > ...17 0H 71 > Mn 71.0 > 91 > Si %Y > Fe %Y > Mo 75 or cobalt %Vo-Y.,0 cobalt 58, 5 “Co %\o—Y “Cr %Yo—0 Mo???1-; containing nickel alloy YO «© % + .) > Cu M > Si%Y) > Mn 961 > Al %Y > Fe %Y > (Ti 9636 > tnickel Nickel %AR=YY,€ for and 96.1 > Zr %or,) > COAY تشغيل مفاعل الطبقة المُميعة ‎fluidized bed reactor‏ لصنع جزيئات مغلفة بالسيليكون ‎silicon-‏Operation of the fluidized bed reactor to make silicon-coated particles ‎.coated particles‏ ‎-١١‏ العملية ‎process‏ وفقا للعنصر ‎VT‏ حيث يتم تغليف ‎coated‏ 96955 على الأقل من السطح ‎surface ©‏ بالطبقة الواقية ‎layer‏ 0106600 مما يقلل أو يزيل إتصال ‎contact‏ الجزئ المغلف بالسيليكون متعدد البلورات ‎polycrystalline silicon-coated particle‏ مع المعدن ‎metal‏ ويقلل ‎reducing‏ أو يزيل التلوث بالمعدن ‎metal‏ لجزئ السيليكون متعدد ‎polycrystalline cys ll‏.coated particles -11 process according to the element VT where at least 96955 of the surface © is coated with the protective layer 0106600 reducing or eliminating the contact of the silicone coated particle polycrystalline silicon-coated particle with metal and reduces reducing or eliminating metal contamination of the polycrystalline cys ll particle ‎.silicon particle‏ ‎—VA Yo‏ الطريقة وفقا لعنصر الحماية ‎V‏ حيث مكون مفاعل الطبقة المُميعة ‎fluidized bed reactor‏ ‎component‏ يكون أنبوب مدخل غاز التمييع ‎ofluidization gas inlet tube‏ مزدوج حراري ‎thermocouple‏ فوهة ضغط ‎«pressure nozzle‏ أو فوهة عينة ‎.sample nozzle‏ ‎COAY‏.silicon particle —VA Yo The method according to claim V, where the fluidized bed reactor component is the ofluidization gas inlet tube, a thermocouple, a pressure nozzle, “ pressure nozzle or .sample nozzle COAY . a A Ej : ‏مي‎ ‎A, i F atoll 1H : 1 EE TRL : LO oF i 4 8 3 i & BOW 8 3 + ES S iN 1 ‏ات‎ ‎H EY : p 3 i ¥ 1 1 3 : ‏لال‎ ‎{ bad H 5 i dof 1 HE EIR § ‏ا‎ ‎ِِ i 0 PWR i : i 1 J i 4 ¥ i 3 i 0 “© Sf I SU SE. a A Ej : M A, i F atoll 1H : 1 EE TRL : LO oF i 4 8 3 i & BOW 8 3 + ES S iN 1 A H EY : p 3 i ¥ 1 1 3 : Lal { bad H 5 i dof 1 HE EIR § a ِ ِ i 0 PWR i : i 1 J i 4 ¥ i 3 i 0 “© Sf I SU SE ‏.ا 0 8 نمسا‎ > 3 7 nl ‏ا‎ ER ‏ا ل‎ 1 i HA i : Hou LI Yaa Ran ¥ 1 ‏اسل ةك با‎ +8 ‏ا ا ل‎ 1 Ey i 1 § ER :A 0 8 Austria > 3 7 nl A ER A L 1 i HA i : Hou LI Yaa Ran ¥ 1 Ask Ba +8 A L 1 Ey i 1 § ER : ¥ . bi] Iv i CO Lhe i : 0: 3 5 : 2 0 1 0 5 EH bad N ‏سسا 0 الاسم‎ #٠ ‏او‎ Hoo dH ‏ب 3 3 + ؟‎ I 3 Hou iy od 0 LOE ‏ا‎ ‎i i ‏#قؤابسسستكت‎ TRS SR I 8 ‏ها‎ HRS 1 ١ § ‏ل‎ ‎i HA BE 0 ‏ف أن‎ - % ¥ ey KR ‏د[ كنك‎ [7[ 3 : ® ‏:م‎ ‎IS H t 3 Et i FEF 4: Hi H 8 i 1 13 I$: 1 1 i 4 qi 4 PR a 4 % I: 3 1 ٠ i NE AW 1 ‏ا‎ ‏ا»» لين‎ ١ ‏اا‎ ‏ض‎ 1 Ls si Fey Sock ‏ا‎ ‎i Rs SO ١ ‏شكل‎ : ‏أي مه‎¥. bi] Iv i CO Lhe i : 0: 3 5 : 2 0 1 0 5 EH bad N Ssa 0 Name #0 or Hoo dH b 3 3 + ? I 3 Hou iy od 0 LOE a i i #Qoabssstct TRS SR I 8 HA HRS 1 1 § l i HA BE 0 q - % ¥ ey KR d [Kenak [7] [ 3 : ® : M IS H t 3 Et i FEF 4: Hi H 8 i 1 13 I$: 1 1 i 4 qi 4 PR a 4 % I: 3 1 0 i NE AW 1 a a “” soft 1 aa z 1 Ls si Fey Sock a i Rs SO 1 form: any meh ل ‎١ : / ١‏ 0 ‏يا‎ ‎1 ‎i = i. ho ‏د‎ EE 0 ‏ا‎ EE 0 0 ‏ا‎ ‎1 ‏ا‎for 1 : / 1 0 O 1 i = i. ho d EE 0 a EE 0 0 a 1 a ‎i. ‎i H i. i ‏م‎ v ‏شكل‎ رمهi. i H i. i m v form rumah + سا لني © ‎A‏ : د ‎a FF‏ :0 82م لاس ض د ٍ 2 11 ض : ‎i‏ ‎|B‏+ s ny © A : d a FF : 0 82m s z d 2 11 z : i |B مدة سريان هذه البراءة عشرون سنة من تاريخ إيداع الطلب وذلك بشرط تسديد المقابل المالي السنوي للبراءة وعدم بطلانها أو سقوطها لمخالفتها لأي من أحكام نظام براءات الاختراع والتصميمات التخطيطية للدارات المتكاملة والأصناف النباتية والنماذج الصناعية أو لائحته التنفيذية صادرة عن مدينة الملك عبدالعزيز للعلوم والتقنية ؛ مكتب البراءات السعودي ص ب ‎TAT‏ الرياض 57؟؟١١‏ ¢ المملكة العربية السعودية بريد الكتروني: ‎patents @kacst.edu.sa‏The validity period of this patent is twenty years from the date of filing the application, provided that the annual financial fee is paid for the patent and that it is not invalid or forfeited for violating any of the provisions of the patent system, layout designs of integrated circuits, plant varieties, and industrial designs, or its executive regulations issued by King Abdulaziz City for Science and Technology; Saudi Patent Office P.O. Box TAT Riyadh 57??11 ¢ Kingdom of Saudi Arabia Email: Patents @kacst.edu.sa
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