03-10-2013 дата публикации
Номер: US20130259770A1
The removal of fluoroalkanes from fluoroalkane-containing hydrocarbon streams, preferably Cto Chydrocarbon streams. The fluoroalkane-containing hydrocarbon stream is contacted with an adsorbent containing a strong acid function, preferably a silica gel or a strong cation ion-exchange resin having sulfonic acid functionality 1. A process for conditioning an adsorbent comprising:(a) providing an adsorbent having strong acid functionality for conditioning;(b) optionally, applying water to the adsorbent;(c) applying an alcohol to the adsorbent; and(d) drying the adsorbent at an elevated temperature.2. The process of claim 1 , wherein the acid functionality of the adsorbent is sulfonic acid.3. The process of claim 1 , wherein the adsorbent is selected from the group consisting of mineral based adsorbents and organic based adsorbents.4. The process of claim 1 , wherein the adsorbent is a mineral based adsorbent selected from the group consisting of zeolites claim 1 , clays claim 1 , and silica gels.5. The process of claim 1 , wherein the adsorbent is comprised of a silica gel with a sulfonic acid functionality.6. The process of claim 1 , wherein the adsorbent is comprised of a polymeric strong cation exchange resin.7. The process of claim 6 , wherein the polymeric strong cation exchange resin is a styrene/divinyl benzene copolymer resin having a sulfonic acid functionality.8. The process of claim 1 , wherein water is applied to the adsorbent prior to the application of the alcohol.9. The process of claim 8 , wherein the alcohol is isopropyl alcohol claim 8 , methanol claim 8 , ethanol claim 8 , n-propanol claim 8 , n-butanol claim 8 , isobutanol claim 8 , sec-butanol claim 8 , or tert-butanol.10. The process of claim 1 , wherein the adsorbent is dried at a temperature of from about 20° C. to about 80° C.11. The process of claim 10 , wherein the adsorbent is dried at a temperature of about 60° C.12. A system for removing fluoroalkanes from a fluoroalkane-containing ...
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