Azeotropic or azeotropic-like compositions of 1,1,1-trifuoroethane and 1-chloro-2,2,2-trifluoroethane
View Patent ↗Azeotropic or azeotropic-like compositions of 1,1,1-trifluoroethane (HFC-143a) and 1-chloro-2,2,2-trifluoroethane (R-133a).
1. An azeotropic or azeotropic-like composition comprising effective amounts of 1,1,1-trifluoroethane (HFC-143a) and 1-chloro-2,2,2-trifluoroethane (R-133a).
2. An azeotropic or azeotropic-like composition according to claim 1 , which consists essentially of effective amounts of 1,1,1-trifluoroethane (HFC-143a) and 1-chloro-2,2,2-trifluoroethane (R-133a).
3. An azeotropic or azeotropic-like composition according to claim 1 which consists essentially of:
from about 70% up to an amount just less than about 100% by weight of HFC-143a, and
from about 30% by weight down to an amount just more than 0% by weight of R-133a,
wherein the weight percentages are based on the total weight of the composition.
4. An azeotropic or azeotropic-like composition according to claim 1 which consists essentially of:
from about 75% to about 99.9% by weight of HFC-143a, and
from about 0.1 to about 25% by weight of R-133a,
wherein the weight percentages are based on the total weight of the composition.
5. An azeotropic or azeotropic-like composition according to claim 1 which consists essentially of:
from about 90% to about 99.9% by weigh of HFC-143a, and
from about 0.1 to about 10% by weigh of R-133a,
wherein the weight percentages are based on the total weight of the composition.
6. An azeotropic or azeotropic-like composition according to claim 1 which has a boiling point of about 46.5±2° C. at an atmospheric pressure of about 14.42 psia.
7. An azeotropic or azeotropic-like composition according to claim 1 which has a boiling point of about −46.6° C. to about −47.2° C. at an atmospheric pressure of about 14.42 psia.
8. An azeotropic or azeotropic-like composition according to claim 1 which has a boiling point of about −46.8° C. to about −47.2° C. at an atmospheric pressure of about 14.42 psia.
9. An azeotropic or azeotropic-like composition according to claim 1 which has a boiling point of about −47° C. to about −47.2° C. at an atmospheric pressure of about 14.42 psia.
10. An azeotropic or azeotropic-like composition according to claim 1 which has a boiling point of about −47.2° C. at an atmospheric pressure of about 14.42 psia.
11. In a process for producing 1,1,1-trifluoroethane (HFC-143a) by the reaction of vinylidene chloride with HF, the improvement comprising purifying the 1,1,1-trifluoroethane (HFC-143a) by distilling off from the product of the reaction an azeotropic or azeotrope-like composition comprising effective amounts of 1,1,1-trifluoroethane (HFC-143a) and 1-chloro-2,2,2-trifluoroethane (R-133a).
12. The process according to claim 11 wherein the azeotropic or azeotrope-like composition distilled from the product of the reaction consists essentially of effective amounts of 1,1,1-trifluoroethane (HFC-143a) and 1-chloro-2,2,2-trifluoroethane (R-133a).
13. The process according to claim 11 wherein the azeotropic or azeotrope-like composition distilled from the product of the reaction consists essentially of: from about 70% by weight up to an amount just less than about 100% by weight of HFC-143a, and from about 30% by weight down to an amount just more than 0% by weight of R-133a, wherein the weight percentages are based on the total weight of the composition.
14. The process according to claim 11 wherein the azeotropic or azeotrope-like composition distilled from the product of the reaction consists essentially of: from about 75% to about 99.9% by weight of HFC-143a, and from about 0.1 to about 25% by weight of R-133a, wherein the weight percentages are based on the total weight of the composition.
15. The process according to claim 11 wherein the azeotropic or azeotrope-like composition distilled from the product of the reaction consists essentially of
from about 90% to about 99.9% by weight of HFC-143a, and
from about 0.1 to about 10% by weight of R-133a,
wherein the weight percentages are based on the total weight of the composition.
16. The process according to claim 11 wherein the azeotropic or azeotrope-like composition distilled from the product of the reaction has a boiling point of about 46.5±2° C. at an atmospheric pressure of about 14.42 psia.
17. The process according to claim 11 wherein the azeotropic or azeotrope-like composition distilled from the product of the reaction has a boiling point of about −46.6° C. to about −47.2° C. at an atmospheric pressure of about 14.42 psia.
18. The process according to claim 11 wherein the azeotropic or azeotrope-like composition distilled from the product of the reaction has a boiling point of about −46.8° C. to about −47.2° C. at an atmospheric pressure of about 14.42 psia.
19. The process according to claim 11 wherein the azeotropic or azeotrope-like composition distilled from the product of the reaction has a boiling point of about −47° C. to about −47.2° C. at an atmospheric pressure of about 14.42 psia.
20. The process according to claim 11 wherein the azeotropic or azeotrope-like composition distilled from the product of the reaction has a boiling point of about −47.2° C. at an atmospheric pressure of about 14.42 psia.
21. The process according to claim 11 wherein the azeotropic or azeotrope-like composition distilled from the product of the reaction is recycled back to the reactor.
22. A process for removing 1-chloro-2,2,2-trifluoroethane (R-133a) impurity from a mixture 1,1,1-trifluoroethane (HFC-143a) and R-133a impurity comprising forming an azeotropic or azeotrope-like composition of the HFC-143a and R-133a and thereafter separating the azeotropic or azeotrope-like composition from the mixture.
23. The process according to claim 22 wherein the separation is conducted by distillation.
24. The process according to claim 22 wherein the azeotropic or azeotrope like composition consists essentially of effective amounts of 1,1,1-trifluoroethane (HFC-143a) and 1-chloro-2,2,2-trifluoroethane (R-133a).
25. The process according to claim 22 wherein the azeotropic or azeotrope-like composition consists essentially of from about 70% by weight up to an amount just less than about 100% by weight of HFC-143a, and from about 30% by weight down to an amount just more than 0% by weight of R-133a, wherein the weight percentages are based on the total weight of the composition.
26. The process according to claim 22 wherein the azeotropic or azeotrope-like composition consists essentially of from about 75% to about 99.9% by weight of HFC-143a, and from about 0.1 to about 25% by weight of R-133a, wherein the weight percentages are based on the total weight of the composition.
27. The process according to claim 22 wherein the azeotropic or azeotrope-like composition consists essentially of from about 90% to about 99.9% by weight of HFC-143a, and from about 0.1 to about 10% by weight of R-133a, wherein the weight percentages are based on the total weight of the composition.
28. The process according to claim 22 wherein the azeotropic or azeotrope-like composition has a boiling point of about 46.5±2° C. at an atmospheric pressure of about 14.42 psia.
29. The process according to claim 22 wherein the azeotropic or azeotrope-like composition has a boiling point of about −46.6° C. to about −47.2° C. at an atmospheric pressure of about 14.42 psia.
30. The process according to claim 22 wherein the azeotropic or azeotrope-like composition has a boiling point of about −46.8° C. to about −47.2° C. at an atmospheric pressure of about 14.42 psia.
31. The process according to claim 22 wherein the azeotropic or azeotrope-like composition has a boiling point of about −47° C. to about −47.2° C. at an atmospheric pressure of about 14.42 psia.
32. The process according to claim 22 wherein the azeotropic or azeotrope-like composition has a boiling point of about −47.2° C. at an atmospheric pressure of about 14.42 psia.
33. A process of distilling a composition comprising HFC-143a and R133a in a distillation column wherein, as a result of the distillation, the R-133a concentration is higher at the top of the column is higher than the concentration of R-133a in the composition at the bottom of the column.