Process for the preparation of 1-chloro-1,1-difluoroethane and/or 1,1,1-trifluoroethane

Claim 2

A process for the fluorination of 1,1,1-trichloroethane comprising reacting 1,1,1-trichloroethane with anhydrous hydrofluoric acid in the presence of antimony pentachloride catalyst in a solvent which meets the following criteria: a. said solvent being capable of dissolving both antimony pentachloride and 1,1,1-trichloroethane; b. said solvent having a boiling point of at least 0° C and a melting point not higher than 60° C; c. said solvent neither reduces antimony pentachloride to a corresponding trivalent antimony compound, nor hydrolyzes antimony pentachloride nor produces a solid complex with antimony pentachloride; d. said solvent being less reactive with anhydrous hydrofluoric acid than methylchloroform or 1,1-dichloro-1-fluoroethane; and e. said solvent being non-reactive with methylchloroform.

Claim 3

The process as defined in claim 1, wherein said solvent is at least one halogenated hydrocarbon having 1 to 4 carbon atoms, said carbon atoms each having 0 to 2 hydrogen atoms.

Claim 4

The process as defined in claim 2, wherein said halogenated hydrocarbon is selected from the group consisting of carbon tetrachloride, chloroform, methylene chloride, trichlorofluoromethane, dichloromonofluoromethane, monochloromonofluoromethane, 1,1,2,2-tetrachloro-2,2-difluoroethane, 1,1,2-trichloro-1,2,2-trifluoroethane, 1,1,1-trichloro-2,2,2-trifluoroethane, 1,2-dichloro-1,2-difluoroethane, 1,1-dichloro-2,2-difluoroethane, 1,1,1,2-tetrachloro-1-fluoroethane, 1,1,2,2-tetrachloro-1-fluoroethane, 1,1,2-trichloro-1,2-difluoroethane, 1,1,2-trichloro-2,2-difluoroethane, 1,1,1-trichloro-2,2-difluoroethane, 1,2-dichloro-1,1,2-trifluoroethane, 1,1-dichloro-1,2,2-trifluoroethane, 1,1-dichloro-2,2,2-trifluoroethane, 1,2-dichloro-1,1,2,2-tetrafluoroethane, 1,1-dichloro-1,2,2,2-tetrafluoroethane, pentachloroethane, 1,2-dichloroethane, 1,1,2-trichloroethane, 1,1,2,2-tetrachloroethane, 1,2-dichloro-1,2,3,3,4,4-hexafluorocyclobutane, 1-chloro-1,2,2,3,3,4,4-heptafluorocyclobutane, 2,3-dichloro-1,1,1,4,4,4-hexafluoro-2-butene, 1,2-dibromo-1,1,2,2-tetrafluoroethane, 1,1,1-trifluoro-2-chloro-2-bromoethane, 1,2-dibromo-1,1,2-trifluoro-2-chloroethane, 1,1,2,2-tetrachloro-1,2-difluoroethane, 1,1,1,2-tetrachloroethane and 1,2,2,3-tetrachloro-1,1,3,3-tetrafluoropropane.

Claim 5

The process as defined in claim 1, wherein said solvent is at least one hydrocarbon selected from the group consisting of chloroform, 1,1,2-trichloro-1,2,2-trifluoroethane, 1,1,2,2-tetrachloro-1,2-difluoroethane, 1,1,1,2-tetrachloroethane, methylene chloride, 1,2-dichloro-1,1,2,2-tetrafluoroethane, trichlorofluoromethane, dichlorofluoromethane, 1,2-dichloroethane, pentachloroethane, 1,1,2,2-tetrachloroethane, 1,2,2,3-tetrachloro-1,1,3,3-tetrafluoropropane, 2,3-dichloro-1,1,1,4,4,4-hexafluoro-2-butene.

Claim 6

The process as defined in claim 1, wherein said catalyst is used in an amount of between 1 and 60% based on the total moles of said catalyst and said solvent.

Claim 7

The process as defined in claim 1, wherein the mole ratio of anhydrous hydrofluoric acid to 1,1,1-trichloroethane ranges from 1.8 to 3.5.

Claim 8

The process as defined in claim 1, wherein said reaction is performed at a temperature of between 0° C. and 80° C.

Claim 9

The process as defined in claim 1, which comprises providing in a reactor a solution of said catalyst in said solvent, bringing simultaneously both anhydrous hydrofluoric acid and 1,1,1-trichloroethane into direct contact with said solution, and recovering a product comprising at least one component selected from 1-chloro-1,1-difluoroethane and 1,1,1-trifluoroethane from the gas emitted from the reactor.

Claim 10

The process as defined in claim 8, wherein the content of said catalyst in the solution ranges from 1 to 60% based on the total moles of said catalyst and said solvent.

Claim 11

The process as defined in claim 8, wherein the mole ratio of anhydrous hydrofluoric acid to 1,1,1-trichloroethane ranges from 1.8 to 3.5.

Claim 12

The process as defined in claim 8, wherein said contacting is by feeding a mixture of anhydrous hydrofluoric acid and 1,1,1-trichloroethane into said solution in the reactor.

Claim 13

The process as defined in claim 8, wherein said recovering step comprises introducing said gas into a first separation zone to separate said gas into a lower boiling point phase and a higher boiling point phase and recovering said product from said lower boiling point phase.

Claim 14

The process as defined in claim 12, wherein said recovering of said product from said lower boiling point phase comprises introducing said lower boiling point phase into a second separation zone to separate said lower boiling point phase into a condensed liquid phase and a gas phase and recovering said product from said gas phase.

Claim 15

The process as defined in claim 12, further comprising recycling said higher boiling point phase into the reactor.

Claim 16

The process as defined in claim 13, further comprising recycling said condensed liquid phase into the first separation zone.