Method of producing 1,1-difluoroethane and application thereof for the production of 1,1-difluoroethylene
View Patent ↗Process for the manufacture of 1,1-difluoroethane by liquid-phase fluorination of 1,2-dichloroethane using hydrofluoric acid in the presence of a Lewis acid as catalyst and of FeCl 3 as cocatalyst. Process for the manufacture of 1,1-difluoroethylene employing it.
1. Process for the manufacture of 1,1-difluoroethane by liquid-phase fluorination of 1,2-dichloroethane using hydrofluoric acid in the presence of a Lewis acid as catalyst, characterized in that the said fluorination is carried out in the presence of FeCl 3 as cocatalyst.
2. Process according to claim 1 , characterized in that use is made of a Lewis acid comprising a compound based on tin, antimony, titanium, molybdenum, tungsten, niobium or tantalum.
3. Process according to claim 1 , characterized in that the Lewis acid is a titanium-based compound.
4. Process according to claim 1 , characterized in that the Lewis acid is a halide, an oxide or an oxyhalide.
5. Process according to claim 1 , characterized in that the Lewis acid is titanium tetrachloride.
6. Process according to claim 1 , characterized in that it is carried out in hydrofluoric acid as solvent.
7. Process according to claim 6 , characterized in that the amount of catalyst to be employed is between 0.0005 and 0.5 mol, preferably between 0.001 and 0.1 mol, per mole of solvent.
8. Process according to claim 1 , characterized in that the cocatalyst/catalyst molar ratio is between 0.01 and 1, preferably between 0.05 and 0.5.
9. Process according to claim 1 , characterized in that its implementation temperature is between 30 and 180° C.
10. Process according to claim 1 , characterized in that its implementation pressure is between 0.2 and 5 MPa absolute.
11. Process according to claim 1 , characterized in that it is carried out continuously.
12. Process for the manufacture of 1,1-difluoroethylene comprising:
(i) the preparation of 1,1-difluoroethane from 1,2-dichloroethane according to the process defined in, then
(ii) the gas-phase chlorination of the 1,1-difluoroethane thus obtained to 1-chloro-1,1-difluoroethane at a temperature of between 30 and 150° C., then
(iii) the gas-phase pyrolysis of the 1-chloro-1,1-difluoroethane thus obtained at a temperature of between 500 and 600° C., and in the absence of catalyst.
13. Process according to claim 6 , characterized in that the amount of catalyst to be employed is between 0.001 and 0.1 mol per mole of solvent.
14. Process according to claim 1 , characterized in that the cocatalyst/catalyst molar ration is between 0.05 and 0.5.
15. Process according to claim 1 , characterized in that its implementation temperature is between 50 and 130° C.
16. Process according to claim 1 , characterized in that its implementation pressure is between 0.5 and 4 MPa absolute.
17. Process according to claim 12 , characterized in that said gas-phase chlorination temperature is between 50 and 120° C.
18. Process according to claim 12 , characterized in that said gas-phase pyrolysis temperature is between 520 and 580° C.