US2013231448A1PendingUtilityA1
Process for separation of tetrafluoroethylene from carbon dioxide using ionic liquids
Est. expiryNov 8, 2026(~0.3 yrs left)· nominal 20-yr term from priority
B01D 3/40C07C 17/38B01D 19/0005C07C 21/185C07D 211/00C07C 17/42C07B 63/00
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Claims
Abstract
A process for separating tetrafluoroethylene from a mixture comprising tetrafluoroethylene and carbon dioxide by contacting the mixture with at least one ionic liquid.
Claims
exact text as granted — not AI-modified1 . A process for separating tetrafluoroethylene from a mixture comprising tetrafluoroethylene and carbon dioxide, comprising contacting the mixture with at least one ionic liquid in which carbon dioxide is soluble to a greater extent than tetrafluoroethylene, and separating the tetrafluoroethylene from the mixture.
2 . The process of claim 1 wherein an ionic liquid has a cation selected from the group consisting of the following eleven cations:
wherein R 1 , R 2 , R 3 , R 4 , R 5 and R 6 are independently selected from the group consisting of:
(i) H
(ii) halogen
(iii) —CH 3 , —C 2 H 5 , or C 3 to C 2 straight-chain, branched or cyclic alkane or alkene, optionally substituted with at least one member selected from the group consisting of Cl, Br, F, I, OH, NH 2 and SH;
(iv) —CH 3 , —C 2 H 5 , or C 3 to C 25 straight-chain, branched or cyclic alkane or alkene comprising one to three heteroatoms selected from the group consisting of O, N and S, and optionally substituted with at least one member selected from the group consisting of Cl, Br, F, I, OH, NH 2 and SH;
(v) C 6 to C 20 unsubstituted aryl, or C 3 to C 25 unsubstituted heteroaryl having one to three heteroatoms independently selected from the group consisting of O, N and S; and
(vi) C 6 to C 25 substituted aryl, or C 3 to C 25 substituted heteroaryl having one to three heteroatoms independently selected from the group consisting of O, N and S; and wherein said substituted aryl or substituted heteroaryl has one to three substituents independently selected from the group consisting of:
(1) —CH 3 , —C 2 H 5 , or C 3 to C 25 straight-chain, branched or cyclic alkane or alkene, optionally substituted with at least one member selected from the group consisting of Cl, Br, F I, OH, NH 2 and SH,
(2) OH,
(3) NH 2 , and
(4) SH;
R 7 , R 8 , R 9 , and R 10 are independently selected from the group consisting of:
(vii) —CH 3 , —C 2 H 5 , or C 3 to C 25 straight-chain, branched or cyclic alkane or alkene, optionally substituted with at least one member selected from the group consisting of Cl, Br, F, I, OH, NH 2 and SH;
(viii)-CH 3 , —C 2 H 5 , or C 3 to C 25 straight-chain, branched or cyclic alkane or alkene comprising one to three heteroatoms selected from the group consisting of O, N and S, and optionally substituted with at least one member selected from the group consisting of Cl, Br, F, I, OH, NH 2 and SH;
(ix) C 6 to C 25 unsubstituted aryl, or C 3 to C 25 unsubstituted heteroaryl having one to three heteroatoms independently selected from the group consisting of O, N and S; and
(x) C 6 to C 25 substituted aryl, or C 3 to C 25 substituted heteroaryl having one to three heteroatoms independently selected from the group consisting of O, N and S; and wherein said substituted aryl or substituted heteroaryl has one to three substituents independently selected from the group consisting of:
(1) —CH 3 , —C 2 H 5 , or C 3 to C 25 straight-chain, branched or cyclic alkane or alkene, optionally substituted with at least one member selected from the group consisting of Cl, Br, F, I, OH, NH 2 and SH,
(2) OH,
(3) NH 2 , and
(4) SH; and
wherein optionally at least two of R 1 , R 2 , R 3 , R 4 , R 5 , R 6 , R 7 , R 8 , R 9 , R 10 can together form a cyclic or bicyclic alkanyl or alkenyl group.
3 . The process of claim 1 wherein at least one of R 1 , R 2 , R 3 , R 4 , R 5 , R 6 , R 7 , R 8 , R 9 , and R 10 comprises F − .
4 . The process of claim 1 wherein an ionic liquid comprises an anion selected from the group consisting of [CH 3 CO 2 ] − , [HSO 4 ] − , [CH 3 OSO 3 ] − , [C 2 HSOSO 3 ] − , [AlCl 4 ] − , [CO 3 ] 2− , [HCO 3 ] − , [NO 2 ] − , [NO 3 ] − , [SO 4 ] 2− , [PO 4 ] 3− , [HPO 4 ] 2− , [H 2 PO 4 ] − , [HSO 3 ] − , [CuCl 2 ] − , Cl − , Br − , I − , SCN − , and any fluorinated anion.
5 . The process of claim 2 wherein an ionic liquid comprises an anion selected from the group consisting of [CH 3 CO 2 ] − , [HSO 4 ] − , [CH 3 OSO 3 ] − , [C 2 H S OSO 3 ] − , [AlCl 4 ] − , [CO 3 ] 2− , [HCO 3 ] − , [NO 2 ] − , [NO 3 ] − , [SO 4 ] 2− , [PO 4 ] 3− , [HPO 4 ] 2− , [H 2 PO 4 ] − , [HSO 3 ] − , [CuCl 2 ] − , Cl − , Br − , I − , SCN − , and any fluorinated anion.
6 . The process of claim 3 wherein an ionic liquid comprises an anion selected from the group consisting of [CH 3 CO 2 ] − , [HSO 4 ] − , [CH 3 OSO 3 ] − , [C 2 HSOSO 3 ] − , [AlCl 4 ] − , [CO 3 ] 2− , [HCO 3 ] − , [NO 2 ] − , [NO 3 ] − , [SO 4 ] 2− , [PO 4 ] 3− , [HPO 4 ] 2− , [H 2 PO 4 ] − , [HSO 3 ] − , [CuCl 2 ] − , Cl − , Br, I − , SCN − , and any fluorinated anion.
7 . The process of claim 1 wherein an ionic liquid comprises an anion selected from the group consisting of [BF] − , [BF 3 CF 3 ] − , [BF 3 C 2 F 5 ] − , [PF 6 ] − , [PF 3 (C 2 F 5 ) 3 ] − , [SbF 6 ] − , [CF 3 SO 3 ] − , [HCF 2 CF 2 SO 3 ] − , [CF 3 HFCCF 2 SO 3 ] − , [HCClFCF 2 SO 3 ] − , [(CF 3 SO 2 ) 2 N] − , [(CF 3 CF 2 SO 2 ) 2 N] − , [(CF 3 SO 2 ) 3 C] − , [CF 3 CO 2 ] − , [CF 3 OCFHCF 2 SO 3 ] − , [CF 3 CF 2 OCFHCF 2 SO 3 ] − , [CF 3 CFHOCF 2 CF 2 SO 3 ] − , [CF 2 HCF 2 OCF 2 CF 2 SO 3 ] − , [CF 2 ICF 2 OCF 2 CF 2 SO 3 ] − , [CF 3 CF 2 OCF 2 CF 2 SO 3 ] − , [CF 2 HCF 2 SO 2 ) 2 N] − , [(CF 3 CFHCF 2 SO 2 ) 2 N] − , and F − .
8 . The process of claim 2 wherein an ionic liquid comprises an anion selected from the group consisting of [BF] − , [BF 3 CF 3 ] − , [BF 3 C 2 F 5 ] − , [PF 6 ] − , [PF 3 (C 2 F 5 ) 3 ] − , [SbF 6 ] − , [CF 3 SO 3 ] − , [HCF 2 CF 2 SO 3 ] − , [CF 3 HFCCF 2 SO 3 ] − , [HCClFCF 2 SO 3 ] − , [(CF 3 SO 2 ) 2 N] − , [(CF 3 CF 2 SO 2 ) 2 N] − , [(CF 3 SO 2 ) 3 C] − , [CF 3 CO 2 ] − , [CF 3 OCFHCF 2 SO 3 ] − , [CF 3 CF 2 OCFHCF 2 SO 3 ] − , [CF 3 CFHOCF 2 CF 2 SO 3 ] − , [CF 2 HCF 2 OCF 2 CF 2 SO 3 ] − , [CF 2 ICF 2 OCF 2 CF 2 SO 3 ] − , [CF 3 CF 2 OCF 2 CF 2 SO 3 ] − , [(CF 2 HCF 2 SO 2 ) 2 N] − , [(CF 3 CFHCF 2 SO 2 ) 2 N] − , and F − .
9 . The process of claim 3 wherein an ionic liquid comprises an anion selected from the group consisting of [BF] − , [BF 3 CF 3 ] − , [BF 3 C 2 F 5 ] − , [PF 6 ] − , [PF 3 (C 2 F 5 ) 3 ] − , [SbF 6 ] − , [CF 3 SO 3 ] − , [HCF 2 CF 2 SO 3 ] − , [CF 3 HFCCF 2 SO 3 ] − , [HCClFCF 2 SO 3 ] − , [(CF 3 SO 2 ) 2 N] − , [(CF 3 CF 2 SO 2 ) 2 N] − , [(CF 3 SO 2 ) 3 C] − , [CF 3 CO 2 ] − , [CF 3 OCFHCF 2 SO 3 ] − , [CF 3 CF 2 OCFHCF 2 SO 3 ] − , [CF 3 CFHOCF 2 CF 2 SO 3 ] − , [CF 2 HCF 2 OCF 2 CF 2 SO 3 ] − , [CF 2 ICF 2 OCF 2 CF 2 SO 3 ] − , [CF 3 CF 2 OCF 2 CF 2 SO 3 ] − , [(CF 2 HCF 2 SO 2 ) 2 N] − , [CF 3 CFHCF 2 SO 2 ) 2 N] − , and F − .
10 . The process of claim 1 wherein an ionic liquid comprises imidazolium as the cation; and comprises an anion selected from the group consisting of [BF] − , [BF 3 CF 3 ] − , [BF 3 C 2 F 5 ] − , [PF 6 ] − , [PF 3 (C 2 F 5 ) 3 ] − , [SbF 6 ] − , [CF 3 SO 3 ] − , [HCF 2 CF 2 SO 3 ] − , [CF 3 HFCCF 2 SO 3 ] − , [HCClFCF 2 SO 3 ] − , [(CF 3 SO 2 ) 2 N] − , [(CF 3 CF 2 SO 2 ) 2 N] − , [(CF 3 SO 2 ) 3 C] − , [CF 3 CO 2 ] − , [CF 3 OCFHCF 2 SO 3 ] − , [CF 3 CF 2 OCFHCF 2 SO 3 ] − , [CF 3 CFHOCF 2 CF 2 SO 3 ] − , [CF 2 HCF 2 OCF 2 CF 2 SO 3 ] − , [CF 2 ICF 2 OCF 2 CF 2 SO 3 ] − , [CF 3 CF 2 OCF 2 CF 2 SO 3 ] − , [(CF 2 HCF 2 SO 2 ) 2 N] − , [(CF 3 CFHCF 2 SO 2 ) 2 N] − , and [CH 3 OSO 3 ] − .
11 . The process of claim 1 wherein an ionic liquid comprises 1-butyl-3-methylimidazolium as the cation; and comprises an anion selected from the group consisting of [BF]—, [BF 3 CF 3 ]—, [BF 3 C 2 F 5 ]—, [PF 6 ]—, [PF 3 (C 2 F 5 ) 3 ]—, [SbF 6 ] − , [CF 3 SO 3 ] − , [HCF 2 CF 2 SO 3 ] − , [CF 3 HFCCF 2 SO 3 ] − , [HCClFCF 2 SO 3 ] − , [(CF 3 SO 2 ) 2 N] − , [(CF 3 CF 2 SO 2 ) 2 N] − , [CF 3 SO 2 ) 3 C] − , [CF 3 CO 2 ] − , [CF 3 OCFHCF 2 SO 3 ] − , [CF 3 CF 2 OCFHCF 2 SO 3 ] − , [CF 3 CFHOCF 2 CF 2 SO 3 ] − , [CF 2 HCF 2 OCF 2 CF 2 SO 3 ] − , [CF 2 ICF 2 OCF 2 CF 2 SO 3 ] − , [CF 3 CF 2 OCF 2 CF 2 SO 3 ] − , [(CF 2 HCF 2 SO 2 ) 2 N] − , [(CF 3 CFHCF 2 SO 2 ) 2 N] − and [CH 3 OSO 3 ] − .
12 . The process of claim 1 wherein an ionic liquid comprises 1-1-ethyl-3-methylimidazolium as the cation; and comprises an anion selected from the group consisting of [BF]—, [BF 3 CF 3 ]—, [BF 3 C 2 F 5 ]—, [PF 6 ]—, [PF 3 (C 2 F 5 ) 3 ]—, [SbF 6 ] − , [CF 3 SO 3 ] − , [HCF 2 CF 2 SO 3 ] − , [CF 3 HFCCF 2 SO 3 ] − , [HCClFCF 2 SO 3 ] − , [(CF 3 SO 2 ) 2 N] − , [(CF 3 CF 2 SO 2 ) 2 N] − , [(CF 3 SO 2 ) 3 C] − , [CF 3 CO 2 ] − , [CF 3 OCFHCF 2 SO 3 ] − , [CF 3 CF 2 OCFHCF 2 SO 3 ] − , [CF 3 CFHOCF 2 CF 2 SO 3 ] − , [CF 2 HCF 2 OCF 2 CF 2 SO 3 ] − , [CF 2 ICF 2 OCF 2 CF 2 SO 3 ] − , [CF 3 CF 2 OCF 2 CF 2 SO 3 ] − , [(CF 2 HCF 2 SO 2 ) 2 N] − , [(CF 3 CFHCF 2 SO 2 ) 2 N] − and [CH 3 OSO 3 ] − .
13 . The process of claim 1 wherein an ionic liquid comprises 1-ethyl-3-methylimidazolium as the cation, and comprises an anion selected from the group consisting of [(CF 3 CF 2 SO 2 ) 2 N] − , [PF 6 ] − and [HCF 2 CF 2 SO 3 ] − .
14 . The process of claim 1 wherein an ionic liquid comprises 1-1,3-dimethylimidazolium as the cation; and comprises an anion selected from the group consisting of [BF 4 ]—, [BF 3 CF 3 ]—, [BF 3 C 2 F 5 ]—, [PF 6 ]—, [PF 3 (C 2 F 5 ) 3 ]—, [SbF 6 ] − , [CF 3 SO 3 ] − , [HCF 2 CF 2 SO 3 ] − , [CF 3 HFCCF 2 SO 3 ] − , [HCClFCF 2 SO 3 ] − , [(CF 3 SO 2 ) 2 N] − , [(CF 3 CF 2 SO 2 ) 2 N] − , [CF 3 SO 2 ) 3 C] − , [CF 3 CO 2 ] − , [CF 3 OCFHCF 2 SO 3 ] − , [CF 3 CF 2 OCFHCF 2 SO 3 ] − , [CF 3 CFHOCF 2 CF 2 SO 3 ] − , [CF 2 HCF 2 OCF 2 CF 2 SO 3 ] − , [CF 2 ICF 2 OCF 2 CF 2 SO 3 ] − , [CF 3 CF 2 OCF 2 CF 2 SO 3 ] − , [(CF 2 HCF 2 SO 2 ) 2 N] − , [(CF 3 CFHCF 2 SO 2 ) 2 N] − and [CH 3 OSO 3 ] − .
15 . The process of claim 1 which is performed in a distillation or absorption column.
16 . The process of claim 15 wherein the TFE is removed from the top of the column.
17 . The process of claim 15 wherein an ionic liquid and CO 2 are removed together from the bottom of the column, the ionic liquid and CO 2 are separated outside the column, and the separated ionic liquid is returned to the column.
18 . A process according to claim 1 further comprising the steps of recovering the TFE, and subjecting the TFE to a polymerization reaction to prepare a fluorinated polymer or copolymer.
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