PROCESS FOR THE PRODUCTION AND PURIFICATION OF TRIFLUOROETHYLENE
The present invention relates to a process for the purification of a fluorocarbon from a mixture comprising said fluorocarbon and hydrogen, said process comprising a stage of bringing said mixture into contact with a membrane M1 to form a stream F1 comprising the fluorocarbon and a stream F2 comprising the hydrogen. The present invention also relates to a process for the production of trifluoroethylene. The present invention also relates to a process for the separation of a hydrofluoroolefin or of a hydrofluoroalkane from nitrogen by membrane separation. The present invention also relates to a process for the separation of trifluoroethylene from chlorotrifluoroethylene or from a hydrofluorocarbon.
1 - 14 . (canceled)
15 . A process for the separation of a mixture comprising trifluoroethylene and a hydrofluorocarbon, said process comprising a stage of bringing said mixture into contact with a membrane M4 to form a stream F9 comprising trifluoroethylene and a stream F10 comprising said hydrofluorocarbon.
16 . The process as claimed in claim 15 , characterized in that said membrane M4 is made of a material selected from the group consisting of polyolefin, polyether, polyimide, polyaramid, polyamide, polysulfone, polyvinylidene fluoride, cellulose, polymethyl methacrylate, polytetrafluoroethylene, polyvinyl fluoride, polychlorotrifluoroethylene, polyethylene-tetrafluoroethylene and tetrafluoroethylene/perfluorovinyl ether copolymer optionally substituted by an SO 3 H group.
17 . The process as claimed in claim 15 , characterized in that said membrane M4 is selected from the group consisting of a film, a laminated structure, hollow fibers, and coated fibers.
18 . The process as claimed in claim 15 , characterized in that said membrane M4 is made of a material selected from the group consisting of polyolefin, polyether, polyimide, and cellulose.
19 . The process as claimed in claim 15 , characterized in that said membrane M4 is made of a material selected from the group consisting of polypropylene, polymethylpentene, cellulose acetate, polyimide, poly[oxy(2,6-dimethyl-1,4-phenylene)] and poly(phenylene oxide).
20 . The process as claimed in claim 15 , characterized in that said membrane M4 is made of polypropylene or polymethylpentene.
21 . The process as claimed in claim 15 , characterized in that said hydrofluorocarbon is a hydrofluoroalkane selected from the group consisting of pentafluoroethane, 1,1,1,2-tetrafluoroethane, 1,1,2,2-tetrafluoroethane, 1,1-difluoroethane, 1,2-difluoroethane, 1,1,2-trifluoroethane, fluoromethane, difluoromethane, trifluoromethane, 1,1,1,2,2-pentafluoropropane, 1,1,1,2,3-pentafluoropropane, 1,1,1,3,3-pentafluoropropane and 1,1,1,2,3,3-hexafluoropropane.
22 . The process as claimed in claim 15 , characterized in that said hydrofluorocarbon is a hydrofluoroalkane selected from the group consisting of pentafluoroethane, 1,1,1,2-tetrafluoroethane, 1,1,2,2-tetrafluoroethane, 1,1-difluoroethane, 1,2-difluoroethane and 1,1,2-trifluoroethane.
23 . The process as claimed in claim 15 , characterized in that said membrane M4 has a selectivity of greater than 10, said selectivity being calculated by the ratio of the permeability of the trifluoroethylene to the permeability of said hydrofluorocarbon through said membrane M4.
24 . The process as claimed in claim 15 , characterized in that said hydrofluorocarbon is a hydrofluoroalkane selected from the group consisting of pentafluoroethane, 1,1,1,2-tetrafluoroethane and 1,1,2,2-tetrafluoroethane, and said membrane M4 is made of polypropylene, polymethylpentene, cellulose acetate, polyimide, poly[oxy(2,6-dimethyl-1,4-phenylene)] or poly(phenylene oxide).
25 . The process as claimed in claim 15 , characterized in that said hydrofluorocarbon is a hydrofluoroalkane selected from the group consisting of pentafluoroethane, 1,1,1,2-tetrafluoroethane and 1,1,2,2-tetrafluoroethane and said membrane M4 is made of polypropylene or polymethylpentene.
26 . A process for the production of trifluoroethylene comprising:
a stage A1) of dehydrofluorination of 1,1,1,2-tetrafluoroethane or a stage of reaction between chlorodifluoromethane and chlorofluoromethane to form a stream comprising trifluoroethylene and a hydrofluorocarbon, and
a stage B1) of separation of a stream comprising trifluoroethylene and a hydrofluorocarbon as claimed in claim 15 with a membrane M4 to form a stream F9′ comprising trifluoroethylene and a stream F10′ comprising said hydrofluorocarbon.
27 . The process as claimed in claim 26 , characterized in that said hydrofluorocarbon is a hydrofluoroalkane selected from the group consisting of pentafluoroethane, 1,1,1,2-tetrafluoroethane and 1,1,2,2-tetrafluoroethane, and said membrane M4 is made of a material selected from the group consisting of polypropylene, polymethylpentene, cellulose acetate, polyimide, poly[oxy(2,6-dimethyl-1,4-phenylene)] and poly(phenylene oxide).
28 . The process as claimed in claim 27 , characterized in that said hydrofluorocarbon is 1,1,1,2-tetrafluoroethane and said membrane M4 is made of a material selected from the group consisting of polypropylene, polymethylpentene, cellulose acetate, polyimide, poly[oxy(2,6-dimethyl-1,4-phenylene)] and poly(phenylene oxide).