Compositional Analysis Of A Gas Or Gas Stream In A Chemical Reactor and Method For Preparing Chlorosilanes In A Fluidized Bed Reactor
US-2016131584-A1 · May 12, 2016 · US
US10933396B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10933396-B2 |
| Application number | US-201816756041-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 16, 2018 |
| Priority date | Nov 20, 2017 |
| Publication date | Mar 2, 2021 |
| Grant date | Mar 2, 2021 |
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Provided is a fluidized bed reactor (1) that makes it possible to stably measure a temperature distribution in the fluidized bed reactor (1) while no damage is caused to a temperature measuring section. Provided is a fluidized bed reactor (1) configured to generate trichlorosilane by reacting metallurgical grade silicon powder and hydrogen chloride gas, the fluidized bed reactor (1) including: a reaction vessel (10); and a plurality of temperature measuring sections (50), provided on an outer surface of the reaction vessel (10), each for measuring a temperature inside the reaction vessel (10).
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The invention claimed is: 1. A fluidized bed reactor configured to generate trichlorosilane by reacting metallurgical grade silicon powder and hydrogen chloride gas, the fluidized bed reactor comprising: a reaction vessel; and a plurality of temperature measuring sections, provided on an outer surface of the reaction vessel, each for measuring a temperature distribution inside the reaction vessel from a temperature of the outer surface of the reaction vessel. 2. The fluidized bed reactor as set forth in claim 1 , wherein the outer surface of the reaction vessel on which outer surface the plurality of temperature measuring sections are provided is located in a vicinity of a gas supply port provided in a lower part of the reaction vessel. 3. The fluidized bed reactor as set forth in claim 2 , wherein the plurality of temperature measuring sections are provided along an entire circumference of the outer surface of the reaction vessel. 4. A fluidized bed reactor as set forth in claim 2 , further comprising: a heating medium pipe provided above the gas supply port in the reaction vessel, the plurality of temperature measuring sections including a temperature measuring section that is provided in a region in which no heating medium pipe is provided. 5. The fluidized bed reactor as set forth in claim 4 , wherein the plurality of temperature measuring sections further include a temperature measuring section that is provided in a region in which the heating medium pipe is provided. 6. A method for producing trichlorosilane by reacting metallurgical grade silicon powder and hydrogen chloride gas, the method comprising: a temperature measuring step of measuring, from a temperature of an outer surface of a reaction vessel of a fluidized bed reactor, a temperature distribution inside the reaction vessel. 7. A method as set forth in claim 6 , further comprising a control step of controlling an amount of supply of hydrogen chloride gas in accordance with a result of the temperature measuring step.
Heating and cooling the reactor (B01J8/42 takes precedence) · CPC title
in a cylindrical shaped bed · CPC title
Sparger-type elements · CPC title
from silicon · CPC title
according to "fluidised-bed" technique (B01J8/20 takes precedence) · CPC title
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