Method for producing trifluoroethylene
View Patent ↗A method to efficiently and stably produce trifluoroethylene from 1,1,1,2-tetrafluoroethane is provided. In the method, a material gas containing 1,1,1,2-tetrafluoroethane in a gaseous phase and calcium oxide in a solid phase are brought into contact with each other in a reactor. Clogging of the reactor is less likely to occur, the load of the moisture removal process is light, and problems such as a decrease in the yield of trifluoroethylene do not arise.
1. A method for producing trifluoroethylene, the method comprising:
contacting a material gas comprising 1,1,1,2-tetrafluoroethane and an inert gas with calcium oxide at a temperature of 200 to 500° C. in a reactor,
wherein a molar ratio of 1,1,1,2-tetrafluoroethane to the inert gas (1,1,1,2-tetrafluoroethane:inert gas) at the contacting is from 20:80 to 100:0, and wherein the inert gas is nitrogen.
2. The method according to claim 1 , wherein the material gas is in a gaseous phase and calcium oxide is in a solid phase.
3. The method according to claim 1 , wherein said contacting occurs at a temperature of 300 to 450° C.
4. The method according to claim 1 , wherein said contacting occurs at a pressure of from 0 to 2 MPa by gauge pressure.
5. The method according to claim 2 , wherein a specific surface area of calcium oxide is from 0.1 to 500 m 2 /g.
6. The method according to claim 1 , wherein the material gas is introduced to a fixed bed reactor packed with calcium oxide.
7. The method according to claim 6 , wherein a contact time of 1,1,1,2-tetrafluoroethane and calcium oxide in the fixed bed reactor is from 0.5 to 20 seconds.
8. The method according to claim 1 , wherein the material gas is introduced to a fluidized bed reactor packed with calcium oxide.
9. The method according to claim 8 , wherein a contact time of 1,1,1,2-tetrafluoroethane and calcium oxide in the fluidized bed reactor is from 0.1 to 20 seconds.
10. The method according to claim 1 , wherein 1,1,1,2-tetrafluoroethane is preheated to a temperature of 80 to 450° C. before 1,1,1,2-tetrafluoroethane is introduced into the reactor.
11. The method according to claim 5 , wherein the specific surface area of calcium oxide is from 1 to 200 m 2 /g.