Catalysts and process to manufacture 2,3,3,3-tetrafluoropropene
View Patent ↗Disclosed is a process for the manufacture of 2,3,3,3-tetrafluoropropene comprising: (a) contacting 1,1,1,2,3-pentafluoropropane with a catalyst comprised of chromium (III) oxide having a surface area of at least 150 m 2 /g and having an alkali metal loading of at least 7 milligrams of alkali metal per 100 square meters of catalyst surface area, to produce a product mixture comprising 2,3,3,3-tetrafluoropropene and hydrogen fluoride; 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) contacting 1,1,1,2,3-pentafluoropropane with a catalyst comprised of chromium (III) oxide having a surface area of at least 150 m 2 /g and having an alkali metal loading of at least 7 milligrams of alkali metal per 100 square meters of catalyst surface area, to produce a product mixture comprising 2,3,3,3-tetrafluoropropene and hydrogen fluoride; and (b) recovering said 2,3,3,3-tetrafluoropropene from the product mixture produced in (a).
2. The process of claim 1 , wherein said alkali metal is potassium.
3. A process of claim 1 , wherein said product mixture comprising 2,3,3,3-tetrafluoropropene comprises less than 20 parts per hundred on a molar basis of 1,1,1,2,2-pentafluoropropane.
4. The 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.
5. The process of claim 1 , wherein the catalyst has a surface area of at least 200 m 2 /g.
6. The process of claim 1 , wherein the catalyst has an alkali metal loading of at least 8 milligrams of alkali metal per 100 square meters of catalyst surface area.
7. The process of claim 1 , wherein the catalyst has an alkali metal loading of at least 9 milligrams of alkali metal per 100 square meters of catalyst surface area.
8. The process of claim 1 , wherein the temperature of the catalyst is maintained at a set point of from 250° C. to 350° C.
9. The process of claim 6 , wherein the temperature of the catalyst is maintained at a set point of from 250° C. to 300° C.