Process to manufacture 2,3,3,3-tetrafluoropropene
Disclosed is a process for the manufacture of 2,3,3,3-tetrafluoropropene comprising: (a) dehydrofluorinating 1,1,1,2,3-pentafluoropropane in the presence of a dehydrofluorination catalyst comprised of chromium (III) oxide, and alkali metal, to produce a product mixture comprising 2,3,3,3-tetrafluoropropene and less than 20 parts per hundred 1,3,3,3-tetrafluoro-1-propene; and (b) recovering said 2,3,3,3-tetrafluoropropene from the product mixture produced in (a).
1. A process for the manufacture of 2,3,3,3-tetrafluoropropene comprising: (a) dehydrofluorinating 1,1,1,2,3-pentafluoropropane in the presence of a dehydrofluorination catalyst comprised of chromium (III) oxide, and an alkali metal in an amount effective to produce a product mixture comprising 2,3,3,3-tetrafluoropropene and less than 20 parts per hundred of 1,1,1,2,2-pentafluoropropane; and (b) recovering said 2,3,3,3 -tetrafluoropropene from the product mixture produced in (a).
2. A process of claim 1 , wherein said product mixture comprising 2,3,3,3-tetrafluoropropene comprises less than 10 parts per hundred on a molar basis of 1,1,1,2,2-pentafluoropropane.
3. The process of claim 1 , wherein said dehydrofluorination catalyst comprises from 0.1% to 2% alkali metal disposed on the surface of said catalyst.
4. The process of claim 1 , wherein said dehydrofluorination catalyst comprises from 0.1% to 1% alkali metal disposed on the surface of said catalyst.
5. The process of claim 1 , wherein said dehydrofluorination catalyst comprises from 0.1% to 1% potassium disposed on the surface of said catalyst.
6. The process of claim 1 , wherein said dehydrofluorination catalyst comprises from 0.5% to 2% alkali metal dispersed throughout the particles of said catalyst.
7. The process of claim 1 , wherein said dehydrofluorination catalyst comprises from 0.1% to 3% boron and at least 3000 ppm of alkali metal.
8. The process of claim 1 , wherein said dehydrofluorination catalyst comprises from 0.5% to 2% boron and at least 3000 ppm of sodium.
9. The process of claim 1 , wherein said dehydrofluorination catalyst comprises from 0.55 to 2% boron and at least 1000 ppm potassium.
10. The process of claim 1 , wherein the temperature of the catalyst is maintained at a set point of from 250° C. to 350° C.
11. The process of claim 8 , wherein the temperature of the catalyst is maintained at a set point of from 250° C. to 300° C.