초록 ▼

A method for the production of 1,1,1,3,3-pentafluoropropene, and particularly to a method characterized by high conversion, yield and selectivity by contacting 2,2-dichloro-1,1,1,3,3,3-hexafluoropropane with hydrogen in the presence of a metal-containing catalyst. The 1,1,1,3,3-pentafluoropropene th

A method for the production of 1,1,1,3,3-pentafluoropropene, and particularly to a method characterized by high conversion, yield and selectivity by contacting 2,2-dichloro-1,1,1,3,3,3-hexafluoropropane with hydrogen in the presence of a metal-containing catalyst. The 1,1,1,3,3-pentafluoropropene then can be reacted with hydrogen in the presence of a metal-containing catalyst to produce 1,1,1,3,3-pentafluoropropane.

대표청구항 ▼

1. A method for the production of 1,1,1,3,3-pentafluoropropene which comprises contacting 2,2-dichloro-1,1,1,3,3,3-hexafluoropropane with hydrogen in the presence of a metal-containing catalyst carried by a carbon support, at a temperature in the range of about 300° C. to about 800° C. and recoverin

1. A method for the production of 1,1,1,3,3-pentafluoropropene which comprises contacting 2,2-dichloro-1,1,1,3,3,3-hexafluoropropane with hydrogen in the presence of a metal-containing catalyst carried by a carbon support, at a temperature in the range of about 300° C. to about 800° C. and recovering the 1,1,1,3,3-pentafluoropropene from the resulting reaction product, wherein the metal-containing catalyst carried by a carbon support is selected from the group consisting of a metal, metal halide, metal oxide, metal oxyhalide and combinations thereof, wherein the metal of the catalyst is selected from the group consisting of Fe, Cu, Ni and Cr. 2. The method of claim 1, wherein the carbon catalyst support is activated carbon. 3. The method of claim 1, wherein said contacting is carried out in a reactor for a period of time between about 0.1 and 60 seconds. 4. The method of claim 1, wherein the molar ratio of hydrogen to 2,2-dichloro-1,1,1,3,3,3-hexafluoropropane is between about 0.1 and about 30. 5. The method of claim 1, wherein the reaction temperature is from about 350° C. to about 800° C. 6. The method of claim 1, wherein the reaction temperature is from about 300° C. to about 500° C. 7. The method of claim 1, wherein the reaction pressure is in the range from ambient to about 450 psi. 8. The method of claim 7, wherein the reaction pressure is in the range of ambient to about 200 psi. 9. A method for the production of 1,1,1,3,3-pentafluoropropane comprising (1) contacting 2,2-dichloro-1,1,1,3,3,3-hexafluoropropane with hydrogen in the presence of a metal-containing catalyst carried by a carbon support, at a temperature in the range of about 300° C. to about 800° C. and recovering 1,1,1,3,3,-pentafluoropropene from the resulting reaction product, and (2) contacting the recovered 1,1,1,3,3-pentafluoropropene with hydrogen in the presence of a metal-containing catalyst carried by a carbon support to produce 1,1,1,3,3-pentafluoropropane. 10. The method of claim 9, wherein the metal-containing catalyst is selected from the group consisting of consisting of a metal, metal halide, metal oxide, metal oxyhalide and combinations thereof. 11. The method of claim 10, wherein the carbon catalyst support is activated carbon. 12. The method of claim 4, wherein the molar ratio of hydrogen to 2,2-dichloro-1,1,1,3,3,3-hexafluoropropane is between about 2 to 8. 13. A method for the production of 1,1,1,3,3-pentafluoro-propene which comprises contacting 2,2-dichloro-1,1,1,3,3,3-hexafluoropropane with hydrogen in the presence of a metal-containing catalyst carried by a carbon support, at a temperature in the range of about 300° C. to about 800° C., and recovering the 1,1,1,3,3-pentafluoropropene from the resulting reaction product, wherein the metal-containing catalyst carried by a carbon-support is selected from the group consisting of a metal, metal halide, metal oxide, metal oxyhalide and combinations thereof, wherein the metal of the catalyst consists of a metal selected from the group consisting of Fe, Cu, Ni and Cr. 14. The method of claim 13, wherein the carbon catalyst support is activated carbon. 15. The method of claim 13, wherein the molar ratio of hydrogen to 2,2-dichloro-1,1,1,3,3,3-hexafluoropropane is between 0.1 and about 30. 16. The method of claim 13, wherein the molar ratio of hydrogen to 2,2-dichloro-1,1,1,3,3,3-hexafluoropropane is between 2 to 8. 17. The method of claim 13, wherein the reaction temperature is from about 300° C. to about 500° C. and the pressure is from ambient to about 450 psi.