Ternary azeotropic or quasi-azeotropic composition comprising HF, 2,3,3,3-tetrafluoropropene and 1,1,1,2,2-pentafluoropropane

1. An azeotropic or quasi-azeotropic composition comprising hydrogen fluoride, 2,3,3,3-tetrafluoropropene and 1,1,1,2,2-pentafluoropropane, wherein said composition has a boiling point between 45° C. and 100° C. at a pressure of 13 to 30 bara.

2. The composition as claimed in claim 1 , wherein the composition is obtained for a pressure greater than 15 bara.

3. The composition as claimed in claim 1 , wherein the composition has a boiling point of between 45° C. and 90° C. at a pressure of between 13 and 28 bara.

4. The composition as claimed in claim 1 , wherein the hydrogen fluoride content is from 10 to 70 mol %, on the basis of the molar composition of said composition.

5. The composition as claimed in claim 1 , wherein the 2,3,3,3-tetrafluoropropene content is from 10 to 90 mol %, on the basis of the molar composition of said composition.

6. The composition as claimed in claim 1 , wherein the 1,1,1,2,2-pentafluoropropane content is from 1 to 50 mol %, on the basis of the molar composition of said composition.

7. The composition as claimed in claim 1 , wherein the boiling point of said azeotropic or quasi-azeotropic composition is between 45° C. and 65° C. at a pressure of between 13 and 20 bara.

8. The composition as claimed in claim 1 , wherein the composition comprises 31 mol % hydrogen fluoride, 66 mol % 2,3,3,3-tetrafluoropropene and 3 mol % 1,1,1,2,2-pentafluoropropane, and has a boiling point of 60° C. at a pressure of 18 bara.

9. The composition as claimed in claim 1 , wherein the composition consists of hydrogen fluoride, 2,3,3,3-tetrafluoropropene and 1,1,1,2,2-pentafluoropropane.

10. A process for separating a composition comprising hydrogen fluoride, 2,3,3,3-tetrafluoropropene and 1,1,1,2,2-pentafluoropropane, wherein the process comprises the steps of:

i) providing a composition comprising hydrogen fluoride, 2,3,3,3-tetrafluoropropene and 1,1,1,2,2-pentafluoropropane;

ii) distilling said composition provided in step i) at a temperature at the bottom of the distillation column below 45° C., and above 0° C., so as to form and recover a first stream, advantageously at the top of the distillation column, comprising 2,3,3,3-tetrafluoropropene and hydrogen fluoride, and a second stream comprising 1,1,1,2,2-pentafluoropropane and hydrogen fluoride; said first stream comprises at least 90% of the 2,3,3,3-tetrafluoropropene present in said composition of step i).

11. The process as claimed in claim 10 , wherein said first stream comprises at least 95% of the 2,3,3,3-tetrafluoropropene present in said composition of step i).

12. The process as claimed in claim 11 , wherein said first stream comprises less than 40% of the 1,1,1,2,2-pentafluoropropane present in said composition of step i).