Method for producing chlorosilane gas using continuous tubular reactor
US-10301182-B2 · May 28, 2019 · US
US9758384B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9758384-B2 |
| Application number | US-201414556590-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 1, 2014 |
| Priority date | Dec 1, 2014 |
| Publication date | Sep 12, 2017 |
| Grant date | Sep 12, 2017 |
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The present invention relates to internals useful for minimizing bubble size in a bubbling fluidized bed reactor. One use for the invention is in an apparatus and method for producing trichlorosilane in which metallurgical grade silicon is reacted with hydrogen chloride gas and while being fluidized by the hydrogen chloride gas, thereby producing trichlorosilane.
Opening claim text (preview).
What is claimed is: 1. A reactor with internals for minimizing bubble size comprising: a reactor with a top, a bottom, and walls between the top and the bottom defining an internal space; a center support in the center of the reactor extending vertically from a bottom part of the reactor to a top part of the reactor; a horizontal top support connected to the center support at the top part of the reactor; a horizontal bottom support connected to the center support at the bottom part of the reactor; a horizontal intermediate support connected to and rotatably adjustable on the center support between the horizontal top support and the horizontal bottom support; and vertically extending internals selected from the group consisting of cables; chains; coils; cords; hinged rods; rods; springs; rods and chains or coils in a linear arrangement connected end to end; and an arrangement of any of the cables, chains, coils, cords, hinged rods, rods, and springs, connected together; extending among the horizontal top support, the horizontal intermediate support and the horizontal bottom support. 2. The reactor with internals for minimizing bubble size according to claim 1 , wherein the vertically extending internals are chains. 3. The reactor with internals for minimizing bubble size according to claim 1 , wherein the horizontal bottom support is connected to the reactor by a plurality of bolts each extending through an arm of the horizontal bottom support to a bolt support member connected to a reactor wall. 4. The reactor with internals for minimizing bubble size according to claim 1 , wherein the horizontal top support is connected to the reactor by a plurality of tapered guide pins each extending through arms of the horizontal top support from a location on a reactor wall. 5. The reactor with internals for minimizing bubble size according to claim 1 , wherein the center support is an all thread rod. 6. A method of minimizing bubble size in a fluidized bed reactor comprising: providing a reactor with internals for minimizing bubble size comprising: a reactor with a top, a bottom, and walls between the top and the bottom defining an internal space; a center support in the center of the reactor extending vertically from a bottom part of the reactor to a top part of the reactor; a horizontal top support connected to the center support at the top part of the reactor; a horizontal bottom support connected to the center support at the bottom part of the reactor; a horizontal intermediate support connected to and rotatably adjustable on the center support between the horizontal top support and the horizontal bottom support; and vertically extending internals selected from the group consisting of cables; chains; coils; cords; hinged rods; rods; springs; rods and chains or coils in a linear arrangement connected end to end; and an arrangement of any of the cables, chains, coils, cords, hinged rods, rods, and springs, connected together; extending among the horizontal top support, the horizontal intermediate support and the horizontal bottom support, supplying metallurgical grade silicon as a raw material to the reactor, introducing hydrogen chloride gas to the reactor to react with the metallurgical grade silicon while the metallurgical grade silicon is fluidized by the hydrogen chloride gas and the metallurgical grade silicon and hydrogen chloride gas flow upward in the reactor, and discharging gas containing trichlorosilane from a top part of the reactor.
inside the bed, e.g. baffles · CPC title
Disengagement zone in fluidised-bed reactors · CPC title
Details of the fluidised bed reactor (B01J8/1836 takes precedence) · CPC title
from silicon · CPC title
Flow distribution elements · CPC title
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