Regeneration vessel adsorption zone and process for adsorbing halogen-containing material and sampling catalyst
US-11724240-B2 · Aug 15, 2023 · US
US2016166986A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016166986-A1 |
| Application number | US-201414905983-A |
| Country | US |
| Kind code | A1 |
| Filing date | Aug 12, 2014 |
| Priority date | Aug 28, 2013 |
| Publication date | Jun 16, 2016 |
| Grant date | — |
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This disclosure relates to a method for purification of off-gas and a device for the same. More particularly, this disclosure relates to a method for purification of off-gas that removes hydrogen chloride from the off-gas discharged after conducting a polysilicon deposition process by chemical vapor deposition, and can separate hydrogen of high purity, and a device for the same.
Opening claim text (preview).
1 . A method for purifying off-gas comprising preparing a carbon support on which a transition metal catalyst is supported; and passing off-gas comprising hydrogen chloride (HCl), hydrogen (H 2 ), and chlorosilane compounds through the carbon support to remove hydrogen chloride. 2 . The method for purifying off-gas according to claim 1 , wherein the transition metal is at least one selected from the group consisting of platinum, palladium, ruthenium, nickel, iridium, rhodium, and compounds thereof. 3 . The method for purifying off-gas according to claim 1 , wherein the carbon support is selected from the group consisting of activated carbon, carbon nanotubes, carbon nanoribbons, carbon nanowires, porous carbon, carbon powder, and carbon black. 4 . The method for purifying off-gas according to claim 1 , wherein the transition meal catalyst is supported in the content of 0.01 to 20 wt %, based on total weight of the carbon support. 5 . The method for purifying off-gas according to claim 1 , wherein the off-gas is gas discharged after conducting a polysilicon deposition process by chemical vapor deposition (CVD). 6 . The method for purifying off-gas according to claim 1 , wherein the off-gas comprises 50 mol % or more of hydrogen, based on the total off-gas. 7 . The method for purifying off-gas according to claim 1 , wherein the chlorosilane compound includes dichlorosilane (SiH 2 Cl 2 ), trichlorosilane (SiHCl 3 ), and silicon tetrachloride (SiCl 4 ). 8 . The method for purifying off-gas according to claim 1 , wherein the content of the hydrogen chloride in the off-gas that has passed through the carbon support is decreased 80% or more, based on the mole number, compared to that before passing through the carbon support. 9 . The method for purifying off-gas according to claim 1 , wherein the step of passing the off-gas through the transition metal catalyst-supported carbon support is conducted under conditions of 20 to 500° C. and 1 to 30 bar. 10 . The method for purifying off-gas according to claim 1 , wherein as the off-gas passes through the transition metal catalyst-supported carbon support, hydrogen chloride is converted into trichlorosilane and silicon tetrachloride. 11 . The method for purifying off-gas according to claim 1 , further comprising separating hydrogen and chlorosilane compounds from the off-gas that has passed through the carbon support. 12 . The method for purifying off-gas according to claim 11 , wherein the step of separating hydrogen and chlorosilane compounds from the off-gas that has passed through the carbon support is conducted by a separation membrane process, a distillation process, a gas liquid separation process, or combinations thereof. 13 . A device for purification of off-gas comprising a catalytic reactor that comprises a transition metal catalyst-supported carbon support, and passes off-gas comprising hydrogen chloride (HCl), hydrogen (H 2 ), and chlorosilane compounds to remove hydrogen chloride; and a separator for separating hydrogen and chlorosilane compounds from the off-gas that has passed through the catalytic reactor. 14 . The device for purification off-gas according to claim 13 , wherein the separator includes at least one selected from the group consisting of a distillation apparatus, a separation membrane apparatus, and a gas liquid separation apparatus.
Halogens or halogen compounds · CPC title
Platinum group metals · CPC title
Nickel · CPC title
from CVD treatment or semi-conductor manufacturing · CPC title
Carbon · CPC title
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