Catalytic production processes for making tetrafluoropropenes and pentafluoropropenes
View Patent ↗A process is disclosed for making CF 3 CF═CHF. The process involves contacting at least one hexafluoropropane selected from the group consisting of CF 3 CF 2 CH 2 F and CF 3 CHFCHF 2 with a chromium oxyfluoride catalyst in a reactor to obtain a product mixture comprising CF 3 CF═CHF, and recovering CF 3 CF═CHF from the product mixture. A process is disclosed for making CF 3 CH═CHF. The process involves contacting CF 3 CH 2 CHF 2 with a chromium oxyfluoride catalyst in a reactor to obtain a product mixture comprising CF 3 CH═CHF, and recovering CF 3 CH═CHF from the product mixture. A process is disclosed for making CF 3 CF═CH 2 . The process involves contacting CF 3 CF 2 CH 3 with a chromium oxyfluoride catalyst in a reactor to obtain a product mixture comprising CF 3 CF═CH 2 , and recovering CF 3 CF═CH 2 from the product mixture.
1. A process comprising: (a) contacting at least one hexafluoropropane selected from the group consisting of 1,1,1,2,2,3-hexafluoropropane and 1,1,1,2,3,3-hexafluoropropane with a chromium oxyfluoride catalyst in a reactor to obtain a product mixture comprising 1,2,3,3,3-pentafluoropropene which includes Z—HFC-1225ye and E-HFC-1225ye and (b) recovering said 1,2,3,3,3-pentafluoropropene from said product mixture wherein the molar ratio of Z—HFC-1225ye to E-HFC-1225ye in said product mixture is at least 6.0.
2. The process of claim 1 wherein said catalyst has surface areas of about 20 m 2 /g to about 500 m 2 /g.
3. The process of claim 1 wherein said catalyst is amorphous.
4. The process of claim 1 wherein said catalyst is prepared from crystalline α-Cr 2 O 3 .
5. The process of claim 1 wherein said catalyst is produced in situ.
6. The process of claim 1 wherein an inert gas is also fed to said reactor.
7. The process of claim 1 wherein a gas comprising oxygen is also fed to said reactor.