Method for separating 1-chloro-3,3,3-trifluoropropene and hydrogen fluoride, and method for producing 1-chloro-3,3,3-trifluoropropene by using same
US-9221732-B2 · Dec 29, 2015 · US
US2016347693A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016347693-A1 |
| Application number | US-201615234409-A |
| Country | US |
| Kind code | A1 |
| Filing date | Aug 11, 2016 |
| Priority date | Feb 20, 2014 |
| Publication date | Dec 1, 2016 |
| Grant date | — |
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To provide a method for purifying trifluoroethylene, by which from a fluid containing trifluoroethylene, a C 1-5 alkane or alkene (excluding trifluoroethylene) in which at least one hydrogen atom may be substituted with a chlorine atom or a fluorine atom can be efficiently removed, and a method for producing trifluoroethylene by which trifluoroethylene can be efficiently produced. A fluid containing trifluoroethylene is brought into contact with at least one type of synthetic zeolite selected from synthetic zeolites 3A, 4A and 5A.
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What is claimed is: 1 . A method for purifying a fluid containing trifluoroethylene, which comprises bringing a fluid containing trifluoroethylene and a C 1-5 alkane or alkene (excluding trifluoroethylene) in which at least one hydrogen atom may be substituted with a chlorine atom or a fluorine atom, into contact with at least one type of synthetic zeolite selected from synthetic zeolites 3A, 4A and 5A to remove the C 1-5 alkane or alkene. 2 . The method for purifying a fluid containing trifluoroethylene according to claim 1 , wherein the C 1-5 alkane or alkene is at least one compound selected from the group consisting of chloromethane, fluoromethane, difluoromethane, chlorofluoromethane, trifluoromethane, chlorodifluoromethane, dichlorodifluoromethane, 1,1,2-trichloro-1,2,2-trifluoroethane, 1,2-dichloro-1,1,2-trifluoroethane, 1-chloro-1,2,2,2-tetrafluoroethane, 1-chloro-1,1,2,2-tetrafluoroethane, pentafluoroethane, 1-chloro-1,2,2-trifluoroethane, 1-chloro-1,1,2-trifluoroethane, 1,1,2,2-tetrafluoroethane, 1,1,1,2-tetrafluoroethane, 2-chloro-1,1-difluoroethane, 1-chloro-1,1-difluoroethane, 1,1,2-trifluoroethane, 1,1,1-trifluoroethane, 1,1-difluoroethane, 1,2-difluoroethane, 1,1,1,2,2,3,3-heptafluoropropane, 1,1,1,2,3,3, 3-heptafluoropropane, 1,1,1,3,3, 3-hexafluoropropane, 1,1,1,2,3,3-hexafluoropropane, E- and/or Z-1,2-difluoroethylene, 1,1-difluoroethylene, fluoroethylene, 3,3-difluoropropene, 3,3,3-trifluoropropene, 2,3,3,3-tetrafluoropropene, E- and/or Z-1,3,3,3-tetrafluoropropene, hexafluoropropene, chlorotrifluoroethylene, 1-chloro-2,2-difluoroethylene, E- and/or Z-1,2-dichlorofluoroethylene, E- and/or Z-1,2-dichloro-1,2-difluoroethylene, tetrafluoroethylene, E- and/or Z-1-chloro-2-fluoroethylene, perfluorocyclobutane, methane, ethane, ethylene, propane, propylene, n-butane, isobutane, 1-n-butene, 2-n-butene and isobutene. 3 . The method for purifying a fluid containing trifluoroethylene according to claim 1 , wherein the C 1-5 alkane or alkene is (E)-1,2-difluoroethylene, and the synthetic zeolite is synthetic zeolite 4A and/or 5A. 4 . The method for purifying a fluid containing trifluoroethylene according to claim 1 , wherein the fluid further contains water, the synthetic zeolite is synthetic zeolite 3A, and water is removed by the contact. 5 . The method for purifying a fluid containing trifluoroethylene according to claim 1 , wherein the synthetic zeolite is one preliminarily subjected to a heat treatment by a dry gas of from 100 to 400° C., or one preliminarily subjected to a heat treatment under reduced pressure. 6 . A method for producing trifluoroethylene, which comprises a purification step of bringing a fluid containing trifluoroethylene and a C 1-5 alkane or alkene (excluding trifluoroethylene) in which at least one hydrogen atom may be substituted with a chlorine atom or a fluorine atom, into contact with at least one type of synthetic zeolite selected from synthetic zeolites 3A, 4A and 5A to purify the fluid. 7 . The method for producing trifluoroethylene according to claim 6 , which comprises a production step of reducing chlorotrifluoroethylene with hydrogen gas in the presence of a catalyst to produce a fluid containing trifluoroethylene and a C 1-5 alkane or alkene (excluding trifluoroethylene) in which at least one hydrogen atom may be substituted with a chlorine atom or a fluorine atom, and the above preparation step. 8 . The method for producing trifluoroethylene according to claim 6 , which comprises a production step of subjecting a composition containing chlorodifluoromethane and/or tetrafluoroethylene and chlorofluoromethane to a synthetic reaction involving heat decomposition in the presence of a heating fluid to produce a fluid containing trifluoroethylene and a C 1-5 alkane or alkene (excluding trifluoroethylene) in which at least one hydrogen atom may be substituted with a chlorine atom or a fluorine atom, and the above purification step. 9 . The method for producing trifluoroethylene according to claim 6 , which comprises a production step of subjecting 1,1,1,2-tetrafluoroethane to dehydrofluorination in the presence of an alkali metal and/or an alkaline earth metal to produce a fluid containing trifluoroethylene and a C 1-5 alkane or alkene (excluding trifluoroethylene) in which at least one hydrogen atom may be substituted with a chlorine atom or a fluorine atom, and the above purification step. 10 . The method for producing trifluoroethylene according to claim 6 , wherein the synthetic zeolite is one preliminarily subjected to a heat treatment by a dry gas of from 100 to 400° C. or one preliminarily subjected to a heat treatment under reduced pressure.
by disproportionation of halogenated hydrocarbons · CPC title
of only halogenated hydrocarbons · CPC title
by hydrogenation · CPC title
by adsorption on solids · CPC title
by dehalogenation · CPC title
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