JPWO2021067379A5 - - Google Patents

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JPWO2021067379A5
JPWO2021067379A5 JP2022519795A JP2022519795A JPWO2021067379A5 JP WO2021067379 A5 JPWO2021067379 A5 JP WO2021067379A5 JP 2022519795 A JP2022519795 A JP 2022519795A JP 2022519795 A JP2022519795 A JP 2022519795A JP WO2021067379 A5 JPWO2021067379 A5 JP WO2021067379A5
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Prior art keywords
condensation reactor
thermal condensation
gas
reaction tubes
heat transfer
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JP2022519795A
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JP2022550404A (en
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Priority claimed from PCT/US2020/053447 external-priority patent/WO2021067379A1/en
Publication of JP2022550404A publication Critical patent/JP2022550404A/en
Publication of JPWO2021067379A5 publication Critical patent/JPWO2021067379A5/ja
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Claims (15)

熱縮合反応器であって、
熱伝達チャンバであって、前記熱伝達チャンバが、第1の方向における流動化ガス流を有する流動床であり、前記熱伝達チャンバが、異なる温度に維持される複数の加熱ゾーンを備える、熱伝達チャンバと、
前記流動化ガス流に対して垂直である第2の方向に前記熱伝達チャンバ内に配設された複数の反応管であって、前記複数の反応管の各々が、前記複数の加熱ゾーンを通過する反応ガス流を有する、複数の反応管と、を備える、熱縮合反応器。
A thermal condensation reactor,
a heat transfer chamber, the heat transfer chamber being a fluidized bed with a fluidized gas flow in a first direction, the heat transfer chamber comprising a plurality of heating zones maintained at different temperatures; a chamber;
a plurality of reaction tubes disposed within the heat transfer chamber in a second direction perpendicular to the fluidizing gas flow, each of the plurality of reaction tubes passing through the plurality of heating zones; A thermal condensation reactor, comprising: a plurality of reaction tubes having a reactant gas flow.
前記流動化ガス流が垂直であり、前記反応ガス流が水平である、請求項1に記載の熱縮合反応器。 The thermal condensation reactor of claim 1, wherein the fluidizing gas flow is vertical and the reactant gas flow is horizontal. シュラウドガスを導入するためのポートをさらに備え、前記シュラウドガスが、前記複数の反応管の各々の一部を通って流れる、請求項1に記載の熱縮合反応器。 The thermal condensation reactor of claim 1, further comprising a port for introducing shroud gas, wherein the shroud gas flows through a portion of each of the plurality of reaction tubes. 前記反応ガスが、塩化ビニルおよびトリクロロシランの混合物であり、前記シュラウドガスが、四塩化ケイ素である、請求項3に記載の熱縮合反応器。 4. The thermal condensation reactor of claim 3, wherein the reaction gas is a mixture of vinyl chloride and trichlorosilane, and the shroud gas is silicon tetrachloride. 前記複数の反応管の各々が、グラファイト、炭素繊維/炭素複合体、炭化ケイ素をコーティングしたイソモールドグラファイト、または炭化ケイ素のいずれかを含む内部ライナと統合されたシーリンググランドと関連付けられる、請求項1に記載の熱縮合反応器。 1 . Each of the plurality of reaction tubes is associated with a sealing gland integrated with an internal liner comprising one of graphite, carbon fiber/carbon composite, isomold graphite coated with silicon carbide, or silicon carbide. Thermal condensation reactor described in . 前記複数の反応管の前記ガス流入口を覆うためのボンネットをさらに備える、請求項1に記載の熱縮合反応器。 The thermal condensation reactor according to claim 1, further comprising a bonnet for covering the gas inlets of the plurality of reaction tubes. 前記複数の反応管の前記ガス流出口を覆うための浮動ヘッドをさらに備え、前記浮動ヘッドが、前記第2の方向に移動可能である、請求項1に記載の熱縮合反応器。 The thermal condensation reactor according to claim 1, further comprising a floating head for covering the gas outlet ports of the plurality of reaction tubes, the floating head being movable in the second direction. 前記浮動ヘッドを含む冷却遷移ユニットをさらに備え、前記冷却遷移ユニットもまた、流動床である、請求項7に記載の熱縮合反応器。 8. The thermal condensation reactor of claim 7, further comprising a cooling transition unit including the floating head, the cooling transition unit also being a fluidized bed. 熱膨張に対応するために、前記熱伝達チャンバと関連付けられた1つ以上のローラ支持体をさらに備える、請求項1に記載の熱縮合反応器。 The thermal condensation reactor of claim 1 further comprising one or more roller supports associated with the heat transfer chamber to accommodate thermal expansion. 前記熱伝達チャンバ内に配設された1つ以上のバッフルをさらに備える、請求項1に記載の熱縮合反応器。 The thermal condensation reactor of claim 1 further comprising one or more baffles disposed within the heat transfer chamber. アルケニル官能性ハロシランを生成するためのプロセスであって、
ハロゲン化アルケニルおよびヒドリド官能性ハロシランを予備混合して、反応ガスを生じさせることと、
前記反応ガスを、流動床内に水平方向に配置された複数の反応管に導入することと、
前記反応ガスに前記流動床内の複数の加熱ゾーンを通過させることであって、前記複数の加熱ゾーンが、異なる温度に維持される、通過させることと、を含む、プロセス。
1. A process for producing alkenyl-functional halosilanes, comprising:
premixing an alkenyl halide and a hydride-functional halosilane to form a reactant gas;
introducing the reaction gas into a plurality of reaction tubes arranged horizontally within the fluidized bed;
passing the reactant gas through a plurality of heating zones within the fluidized bed, the plurality of heating zones being maintained at different temperatures.
前記ヒドリド官能性ハロシランおよびハロゲン化水素のハロゲン化生成物を含むシュラウドガスで前記反応ガスを希釈することをさらに含む、請求項11に記載のプロセス。 12. The process of claim 11, further comprising diluting the reactant gas with a shroud gas comprising the hydride-functional halosilane and a halogenated product of hydrogen halide. 前記ハロゲン化アルケニルが、塩化ビニルである、請求項11または12に記載のプロセス。 13. A process according to claim 11 or 12, wherein the alkenyl halide is vinyl chloride. 前記ヒドリド官能性ハロシランが、化学式RSiX(4-w-x)を有し、ここで、添え字、添え字wが、0~2であり、添え字xが、1~3であり、量(w+x)が、1~3であり、各Rが、脂肪族不飽和のない1~18個の炭素原子の、独立して選択された一価の炭化水素族であり、各Xが、独立して選択されたハロゲン原子である、請求項11または12に記載のプロセス。 The hydride-functional halosilane has the formula R w H x SiX (4-w-x) , where the subscript w is from 0 to 2 and the subscript x is from 1 to 3. and the amount (w+x) is from 1 to 3, each R is an independently selected monovalent hydrocarbon group of 1 to 18 carbon atoms without aliphatic unsaturation, and each 13. A process according to claim 11 or 12 , wherein are independently selected halogen atoms. 前記ヒドリド官能性ハロシランが、トリクロロシランである、請求項14に記載のプロセス。 15. The process of claim 14, wherein the hydrido-functional halosilane is trichlorosilane.
JP2022519795A 2019-10-01 2020-09-30 Thermal condensation reactor Pending JP2022550404A (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US201962908802P 2019-10-01 2019-10-01
US62/908,802 2019-10-01
PCT/US2020/053447 WO2021067379A1 (en) 2019-10-01 2020-09-30 Thermal condensation reactor

Publications (2)

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JP2022550404A JP2022550404A (en) 2022-12-01
JPWO2021067379A5 true JPWO2021067379A5 (en) 2023-10-12

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JP2022519795A Pending JP2022550404A (en) 2019-10-01 2020-09-30 Thermal condensation reactor

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US (1) US20220401907A1 (en)
EP (1) EP4038077B1 (en)
JP (1) JP2022550404A (en)
CN (1) CN114502271B (en)
WO (1) WO2021067379A1 (en)

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4197907A (en) * 1978-04-05 1980-04-15 Exxon Research & Engineering Co. Floating head support system for shell and tube heat exchanger
CA1320035C (en) * 1986-08-20 1993-07-13 William Terry Strange Process for preparing halosilanes
EP0841342B1 (en) * 1996-11-06 2001-11-28 Degussa AG Process for the preparation of vinyl-trichlorosilane
FI110205B (en) * 1998-10-02 2002-12-13 Foster Wheeler Energia Oy Method and apparatus in a fluidized bed heat exchanger
DE10319625B3 (en) * 2003-05-02 2004-10-14 Outokumpu Oyj Heat treating solids, preferably iron oxide-containing solids, in a fluidized bed reactor comprises passing fluidizing gas through distribution plates to fluidize the solids
US7569086B2 (en) * 2006-04-24 2009-08-04 Thermochem Recovery International, Inc. Fluid bed reactor having vertically spaced apart clusters of heating conduits
CN100439313C (en) * 2006-10-27 2008-12-03 清华大学 Multistage fluidized bed reactor for preparing propenoic acid from propene oxidation and preparing method

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