System and method of co2 thermal swing adsorption with wet regeneration and hot drying
US-2024058740-A1 · Feb 22, 2024 · US
US2017120184A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2017120184-A1 |
| Application number | US-201514770063-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jun 25, 2015 |
| Priority date | Jul 3, 2014 |
| Publication date | May 4, 2017 |
| Grant date | — |
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Gaseous perfluorocarbons in a waste gas are adsorbed by an adsorption device. Subsequently a decomposition of the perfluorocarbons takes place with formation of hydrogen fluoride. The hydrogen fluoride is converted with an oxide of a metal to be reduced, to the metal fluoride thereof. The metal fluoride formed is then fed again to the reduction process.
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1 - 9 . (canceled) 10 . A method for cleaning a waste gas from a metal reduction process, comprising: adsorbing gaseous perfluorocarbons in the waste gas by an adsorption device; forming hydrogen fluoride by decomposing the perfluorocarbons obtained from said adsorbing; converting the hydrogen fluoride, using an oxide of a metal to be reduced, to a metal fluoride of the metal to be reduced; and feeding the metal fluoride formed by said converting to the metal reduction process. 11 . The method as claimed in claim 10 , further comprising detecting perfluorocarbons by a sensor system, and wherein the waste gas is supplied to the adsorption device if a pre-set limit value of the gaseous perfluorocarbons is exceeded. 12 . The method as claimed in claim 10 , wherein the adsorption device is operated according to a pressure swing adsorption principle. 13 . The method as claimed in claim 10 , wherein the adsorption device is operated according to a temperature swing adsorption principle. 14 . The method as claimed in claim 10 , wherein adsorption materials in the adsorption device are selected from the group consisting of activated carbon, carbon nanotubes and a molecular sieve. 15 . The method as claimed in claim 10 , wherein adsorption materials in the adsorption device include silicalite-1. 16 . The method as claimed in claim 10 , wherein said forming of the hydrogen fluoride is by thermally decomposing the perfluorocarbons. 17 . The method as claimed in claim 10 , wherein the perfluorocarbons are decomposed by a plasma device. 18 . The method as claimed in claim 10 , wherein said adsorbing uses at least two adsorption devices, and wherein said method further comprises alternately charging and discharging the at least two adsorption devices. 19 . The method as claimed in claim 10 , further comprising discharging the adsorption device by at least one of a temperature change and a pressure change.
of perfluorocarbons [PFC], hydrofluorocarbons [HFC] or sulfur hexafluoride [SF6] · CPC title
Molecular sieves other than zeolites · CPC title
Employing electrical discharges or the generation of a plasma · CPC title
Carbon · CPC title
of sorbents or filter aids comprising free carbon, e.g. activated carbon · CPC title
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