Selectively reacting olefins having a terminal CF2 group in a mixture
A process is disclosed for reducing the mole ratio of (1) compounds of the formula Y 1 Y 2 C═CF 2 wherein Y 1 and Y 2 are each independently H, F, Cl, Br, C 1 -C 6 alkyl or C 1 -C 6 haloalkyl containing no more than 3 chlorine substituents, 2 bromine substituents and 1 iodo substituent to (2) saturated compounds of the formula C d H e F f Cl g Br h I k wherein d is an integer from 1 to 10, and e+f+g+h+k is equal to 2d+2, provided that g is 0, 1, 2 or 3, h is 0, 1 or 2 and k is 0 or 1 and/or unsaturated compounds of the formula Y 3 Y 4 C═CY 5 Y 6 , wherein Y 3 , Y 5 and Y 6 are each independently H, F, Cl, Br, C 1 -C 6 alkyl or C 1 -C 6 haloalkyl containing no more than 3 chlorine substituents, 2 bromine substituents and 1 iodo substituent, provided that Y 5 and Y 6 are not both F, and Y 4 is C 1 -C 6 alkyl or C 1 -C 6 haloalkyl containing no more than 3 chlorine substituents, 2 bromine substituents and 1 iodo substituent, in a mixture. The process involves contacting the mixture with at least one selective removal agent selected from the group consisting of SO 3 and RSO 3 H, wherein R is selected from the group consisting of F, Cl, OH, C 1 -C 8 alkyl, C 1 -C 8 fluoroalkyl, and C 1 -C 8 fluoroalkoxyalkyl containing no more than two ether oxygens to selectively react the formula Y 1 Y 2 C═CF 2 compounds.
1. A process for reducing the mole ratio of a (1) first component selected from the group consisting of compounds of the formula Y 1 Y 2 C═CF 2 wherein Y 1 and Y 2 are each independently H, F, Cl, Br, C 1 -C 6 alkyl or C 1 -C 6 haloalkyl containing no more than 3 chlorine substituents, 2 bromine substituents and 1 iodo substituent to a (2) second component selected from the group consisting of saturated compounds of the formula C d H e F f Cl g Br h I k wherein d is an integer from 1 to 10, and e+f+g+h+k is equal to 2d+2, provided that g is 0, 1, 2 or 3, h is 0, 1 or 2 and k is 0 or 1 and unsaturated compounds of the formula Y 3 Y 4 C═CY 5 Y 6 , wherein Y 3 , Y 5 and Y 6 are each independently H, F, Cl, Br, C 1 -C 6 alkyl or C 1 -C 6 haloalkyl containing no more than 3 chlorine substituents, 2 bromine substituents and 1 iodo substituent, provided that Y 5 and Y 6 are not both F, and Y 4 is C 1 -C 6 alkyl or C 1 -C 6 haloalkyl containing no more than 3 chlorine substituents, 2 bromine substituents and 1 iodo substituent, in a mixture comprising said first component and second component, comprising:
contacting said mixture with at least one selective removal agent selected from the group consisting of SO 3 and RSO 3 H, wherein R is selected from the group consisting of F, Cl, OH, C 1 -C 8 alkyl, C 1 -C 8 fluoroalkyl, and C 1 -C 8 fluoroalkoxyalkyl containing no more than two ether oxygens to selectively react said selective removal agent with said first component.
2. The process of claim 1 wherein the component (1) compounds are selected from the group consisting of 1,1,3,3,3-pentafluoropropene (HFC-1225zc), trifluoroethylene (HFC-1123), tetrafluoroethylene (TFE), chlorotrifluoroethylene (CTFE), 1-chloro-2,2-difluoroethene, 2-chloro-1,1,3,3,3-pentafluoro-1-propene (CFC-1215xc), 2-bromo-1,1,3,3,3-pentafluoro-1-propene (CFC-1215xcB), hexafluoropropene (HFP), and perfluoroisobutylene (PFIB), 1,1,2,3,3-pentafluoro-1-propene, 1,1,2,3-tetrafluoro-1-propene, 1,1,3,3-tetrafluoro-1-propene, 1,1,2-trifluoro-1-propene, and 1,1,3-trifluoro-1-propene.
3. The process of claim 1 wherein the saturated component (2) compounds are selected from the group consisting of difluoromethane (HFC-32), trifluoromethane (HFC-23), fluoroethane (HFC-161), 1,1-difluoroethane (HFC-152a), 1,1,1-trifluoroethane (HFC-143a), 1,1,1,2-tetrafluoroethane (HFC-134a), 1,1,2,2-tetrafluoroethane (HFC-134), 1,1,1,2,2-pentafluoroethane (HFC-125), 1,1,1,3,3,3-hexafluoropropane (HFC-236fa), 1,1,1,2,3,3-hexafluoropropane (HFC-236ea), 1,1,2,2,3,3-hexafluoropropane (HFC-236ca), 1,1,1,2,2,3-hexafluoropropane (HFC-236cb), 1,1,1,2,2,3,3-heptafluoropropane (HFC-227ca), 1,1,1,2,3,3,3-heptafluoropropane (HFC-227ea), 1,1,1,3,3-pentafluoropropane (HFC-245fa), 1,1,1,2,2-pentafluoropropane (HFC-245cb), 1,1,2,2,3-pentafluoropropane (HFC-245ca), 1,1,2,3,3-pentafluoropropane (HFC-245ea), 1,1,1,2,3-pentafluoropropane (HFC-245eb), 1,1,1,2-tetrafluoropropane (HFC-254eb), 1,1,1,3-tetrafluoropropane (HFC-254fb), and 1,1,1-trifluoropropane (HFC-263fb).
4. The process of claim 1 wherein the unsaturated component (2) compounds are selected from the group consisting of 1,3,3,3-tetrafluoro-1-propene (HFC-1234ze), 2,3,3,3-tetrafluoro-1-propene (HFC-1234yf), 1,2,3,3,3-pentafluoro-1-propene (HFC-1225ye), 1,1,1,4,4,4-hexafluoro-2-butene (HFC-1338m/z), 1,1,1,3,4,4,5,5,5-nonafluoro-2-pentene (HFC-1429mzy), 1,1,1,2,4,4,5,5,5-nonafluoro-2-pentene (HFC-1429myz), 1,1,1,3,3,4,4,4-octafluoro-2-pentene (HFC-1438m/z), 2-chloro-3,3,3-trifluoro-1-propene, 1,2,2-trichloro-3,3,3-trifluoro-1-propene, 1,2-dichloro-3,3,3-trifluoro-1-propene, 1,2,3,3-tetrafluoro-1-propene, and 3,3,3-trifluoro-1-propene.
5. The process of claim 1 wherein said selective removal agent is selected from the group consisting of SO 3 , oleum, fluorosulfonic acid, chlorosulfonic acid, trifluoromethanesulfonic acid, 1,1,2,2-tetrafluoroethanesulfonic acid, 1,1,1,2-tetrafluoroethanesulfonic acid, 1,1,1,2,3,3-hexafluoropropane sulfonic acid, and methane sulfonic acid.
6. The process of claim 1 wherein said reaction is carried out at a temperature from about 20° C. to about 50° C.
7. The process of claim 1 wherein the component (2) compounds are unsaturated compounds.
8. The process of claim 7 wherein the reaction of the selective removal agent and the component (1) compound forms a fluorine-containing β-sultone or a sulfate.
9. The process of claim 8 wherein component (1) is trifluoroethylene, 1,1,3,3,3-pentafluoropropene or a mixture thereof, component (2) is 1,2,3,3,3-pentafluoro-1-propene, and said selective removal agent is selected from the group consisting of SO 3 , oleum, fluorosulfonic acid, chlorosulfonic acid, trifluoromethanesulfonic acid, 1,1,2,2-tetrafluoroethanesulfonic acid, 1,1,1,2-tetrafluoroethanesulfonic acid, and 1,1,1,2,3,3-hexafluoropropane sulfonic acid.
10. A process for recovering at least one product compound selected from the group consisting of saturated compounds of the formula C d H e F f Cl g Br h I k wherein d is an integer from 1 to 10, and e+f+g+h+k is equal to 2d+2, provided that g is 0, 1, 2 or 3, h is 0, 1 or 2 and k is 0 or 1 and unsaturated compounds of the formula Y 3 Y 4 C═CY 5 Y 6 , wherein Y 3 , Y 5 and Y 6 are each independently H, F, Cl, Br, C 1 -C 6 alkyl or C 1 -C 6 haloalkyl containing no more than 3 chlorine substituents, 2 bromine substituents and 1 iodo substituent, provided that Y 5 and Y 6 are not both F, and Y 4 is C 1 -C 6 alkyl or C 1 -C 6 haloalkyl containing no more than 3 chlorine substituents, 2 bromine substituents and 1 iodo substituent from a mixture comprising (i) said at least one product compound and (ii) olefinic impurity selected from the group consisting of compounds of the formula Y 1 Y 2 C═CF 2 wherein Y 1 and Y 2 are each independently H, F, Cl, Br, C 1 -C 6 alkyl or C 1 -C 6 haloalkyl containing no more than 3 chlorine substituents, 2 bromine substituents and 1 iodo substituent, comprising:
(a) contacting said mixture with at least one selective removal agent selected from the group consisting of SO 3 and RSO 3 H, wherein R is selected from the group consisting of F, Cl, OH, C 1 -C 8 alkyl, C 1 -C 8 fluoroalkyl, and C 1 -C 8 fluoroalkoxyalkyl containing no more than two ether oxygens to selectively react said selective removal agent with said olefinic impurity, thereby reducing the ratio of olefinic impurity to said at least one product compound; and
(b) separating said at least one product from the reaction product of the olefinic impurity with the selective removal agent produced in (a).