Process for preparing a c3-c7 (hydro) fluoroalkene by dehydrohalogenation
US-2015126786-A1 · May 7, 2015 · US
US12083493B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12083493-B2 |
| Application number | US-202117192421-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 4, 2021 |
| Priority date | Mar 4, 2021 |
| Publication date | Sep 10, 2024 |
| Grant date | Sep 10, 2024 |
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Methods for purification of a fluorocarbon or hydrofluorocarbon containing at least one undesired halocarbon impurities comprise flowing the fluorocarbon or hydrofluorocarbon through at least one adsorbent beds to selectively adsorb the at least one undesired halocarbon impurities through physical adsorption and/or chemical adsorption, wherein the at least one adsorbent beds contain a metal oxide supported on an adsorbent in an inert atmosphere.
Opening claim text (preview).
We claim: 1. A process for purification of a fluorocarbon or hydrofluorocarbon containing at least one undesired halocarbon impurities, comprising: flowing the fluorocarbon or hydrofluorocarbon through at least one adsorbent beds to selectively adsorb the at least one undesired halocarbon impurities through physical adsorption and/or chemical adsorption, wherein the at least one adsorbent beds contain a metal oxide MgO supported on an adsorbent in an inert atmosphere; and regenerating the at least one adsorbent beds after the selective adsorption at a temperature ranging from 500° C. to 1000° C. with continuously flowing a purge gas through the at least one adsorbent beds, wherein the purge gas is either pure H 2 or H 2 in balance an inert gas selected from He, N 2 , Ar, Xe or Kr. 2. The process of claim 1 , further comprising: distilling an outlet stream of the at least one adsorption beds to obtain a purified fluorocarbon or hydrofluorocarbon. 3. The process of claim 1 , wherein the at least one undesired halocarbon impurities are Cl-containing, Br-containing, I-containing, or combinations thereof halocarbons. 4. The process of claim 3 , wherein the at least one undesired halocarbon impurities are chlorofluorocarbons (CFC) and/or hydrochlorofluorocarbons (HCFC). 5. The process of claim 1 , wherein the adsorbent is silica, alumina or molecular sieves. 6. The process of claim 1 , wherein a flow rate of the fluorocarbon or hydrofluorocarbon into the at least one adsorbent beds in vapor phase ranges from 0.5 standard liter per minute (SLM) to 500 standard liter per minute (SLM). 7. The process of claim 1 , wherein a temperature of the at least one adsorbent beds ranges from −50° C. to 150° C. 8. The process of claim 2 , wherein a concentration of impurities in the purified fluorocarbon or hydrofluorocarbon is less than 1000 ppm. 9. A process for purification of a fluorocarbon or hydrofluorocarbon containing at least one undesired halocarbon impurities, comprising: flowing the fluorocarbon or hydrofluorocarbon through at least one adsorbent beds to selectively adsorb the at least one undesired halocarbon impurities through physical adsorption and/or chemical adsorption, wherein the at least one adsorbent beds contain a metal oxide MgO supported on an adsorbent in an inert atmosphere; regenerating the at least one adsorbent beds after the selective adsorption at a temperature ranging from 500° C. to 1000° C. with a purge gas containing either pure H 2 or H 2 in balance an inert gas selected from He, N 2 , Ar, Xe or Kr; and distilling an outlet stream of the at least one adsorption beds to obtain a purified fluorocarbon or hydrofluorocarbon. 10. The process of claim 9 , wherein a concentration of impurities in the purified fluorocarbon or hydrofluorocarbon is less than 1000 ppm. 11. The process of claim 9 , wherein the at least one undesired halocarbon impurities are Cl-containing, Br-containing, I-containing, or combinations thereof halocarbons.
in the gas phase · CPC title
by using a purge gas (B01D2259/4009 takes precedence) · CPC title
Fluorine · CPC title
Chlorine · CPC title
Halogens or halogen compounds · CPC title
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