Azeotrope or azeotrope-like compositions of trifluoroiodomethane (CF
The present disclosure provides azeotrope or azeotrope-like compositions including trifluoroiodomethane (CF 3 I) and hexafluoroacetone (HFA), and a method of forming an azeotrope or azeotrope-like composition comprising the step of combining hexafluoroacetone (HFA) and trifluoroiodomethane (CF 3 I) to form an azeotrope or azeotrope-like comprising hexafluoroacetone (HFA) and trifluoroiodomethane (CF 3 I) having a boiling point of about −29.84° C.±0.30° C. at a pressure of about 14.40 psia±0.30 psia.
1. A composition comprising an azeotrope or azeotrope-like composition consisting essentially of effective amounts of hexafluoroacetone (HFA) and trifluoroiodomethane (CF 3 I).
2. The composition of claim 1 , wherein the azeotrope or azeotrope-like composition has a boiling point of about −29.84° C.±0.30° C. at a pressure of about 14.40 psia±0.30 psia.
3. The composition of claim 1 , wherein the azeotrope of azeotrope-like composition consists essentially of from about 28 wt. % to about 75 wt. % hexafluoroacetone (HFA) and from about 25 wt. % to about 72 wt. % trifluoroiodomethane (CF 3 I).
4. The composition of claim 1 , wherein the azeotrope or azeotrope-like composition consists essentially of from about 45 wt. % to about 70 wt. % hexafluoroacetone (HFA) and from about 30 wt. % to about 55 wt. % trifluoroiodomethane (CF 3 I).
5. The composition of claim 1 , wherein the azeotrope or azeotrope-like composition consists essentially of from about 59 wt. % to about 60 wt. % hexafluoroacetone (HFA) and from about 40 wt. % to about 41 wt. % trifluoroiodomethane (CF 3 I).
6. The composition of claim 1 , wherein the azeotrope or azeotrope-like composition consists essentially of about 59.78 wt. % hexafluoroacetone (HFA) and about 40.22 wt. % trifluoroiodomethane (CF 3 I).
7. A composition comprising an azeotrope or azeotrope-like composition consisting essentially of hexafluoroacetone (HFA) and trifluoroiodomethane (CF 3 I) and having a boiling point of about −29.84° C.±0.30° C. at a pressure of about 14.40 psia±0.30 psia.
8. The composition of claim 7 , wherein the azeotrope or azeotrope-like composition consists essentially of from about 28 wt. % to about 75 wt. % hexafluoroacetone (HFA) and from about 25 wt. % to about 72 wt. % trifluoroiodomethane (CF 3 I).
9. The composition of claim 7 , wherein the azeotrope or azeotrope-like composition consists essentially of from about 45 wt. % to about 70 wt. % hexafluoroacetone (HFA) and from about 30 wt. % to about 55 wt. % trifluoroiodomethane (CF 3 I).
10. The composition of claim 7 , wherein the azeotrope or azeotrope-like composition consists essentially of from about 59 wt. % hexafluoroacetone (HFA) to about 60 wt. % hexafluoroacetone and from about 40 wt. % trifluoroiodomethane (CF 3 I) to about 41 wt % trifluoroiodomethane (CF 3 I).
11. The composition of claim 7 , wherein the azeotrope or azeotrope-like composition consists essentially of about 59.78 wt. % hexafluoroacetone (HFA) and about 40.22 wt. % trifluoroiodomethane (CF 3 I).
12. The composition of claim 7 , wherein the azeotrope or azeotrope-like composition consists of from about 28 wt. % to about 75 wt. % hexafluoroacetone (HFA) and from about 25 wt. % to about 72 wt. % trifluoroiodomethane (CF 3 I).
13. The composition of claim 7 , wherein the azeotrope or azeotrope-like composition consists of from about 45 wt. % to about 70 wt. % hexafluoroacetone (HFA) and from about 30 wt. % to about 55 wt. % trifluoroiodomethane (CF 3 I).
14. The composition of claim 7 , wherein the azeotrope or azeotrope-like composition consists of about 59.78 wt. % hexafluoroacetone (HFA) and about 40.22 wt. % trifluoroiodomethane (CF 3 I).
15. A method of forming an azeotrope or azeotrope-like composition comprising the step of combining hexafluoroacetone (HFA) and trifluoroiodomethane (CF 3 I) to form an azeotrope or azeotrope-like composition consisting essentially of hexafluoroacetone (HFA) and trifluoroiodomethane (CF 3 I) having a boiling point of about −29.84° C.±0.30° C. at a pressure of about 14.40 psia±0.30 psia.
16. The method of claim 15 , wherein the combining step comprises combining from about 28 wt. % to about 75 wt. % hexafluoroacetone (HFA) and from about 25 wt. % to about 72 wt. % trifluoroiodomethane (CF 3 I).
17. The method of claim 15 , wherein the combining step comprises combining from about 45 wt. % to about 70 wt. % hexafluoroacetone (HFA) and from about 30 wt. % to about 55 wt. % trifluoroiodomethane (CF 3 I).
18. The method of claim 15 , wherein the combining step comprises combining about 59.78 wt. % hexafluoroacetone (HFA) and about 40.22 wt. % trifluoroiodomethane (CF 3 I).
19. A method of separating hexafluoroacetone (HFA) and trifluoroiodomethane (CF 3 I) from a primary composition comprising hexafluoroacetone (HFA), trifluoroiodomethane (CF 3 I) and at least one impurity, including the steps of:
forming, within the primary composition, a secondary composition which is an azeotrope or azeotrope-like composition consisting essentially of effective amounts of hexafluoroacetone (HFA) and trifluoroiodomethane (CF 3 I) having a boiling point of about −29.84° C.±0.30° C. at a pressure of about 14.40 psia±0.30 psia; and
separating the secondary composition from the primary composition at least one impurity.
20. The method of claim 19 , wherein the forming step comprises forming, within the primary composition, a secondary composition which is an azeotrope or azeotrope-like composition consisting essentially of from about 28 wt. % to about 75 wt. % hexafluoroacetone (HFA) and from about 25 wt. % to about 72 wt. % trifluoroiodomethane (CF 3 I) and having a boiling point of about −29.84° C.±0.30° C. at a pressure of about 14.40 psia±0.30 psia.