Isomerization of 1-chloro-3,3,3-trifluoropropene
View Patent ↗Disclosed are processes for an isomerization reaction between (E)1-chloro-3,3,3-trifluoropropene and (Z)1-chloro-3,3,3-trifluoropropene. Some of the disclosed processes include the step of contacting a feed stream with a heated surface, where the feed stream includes (E)1-chloro-3,3,3-trifluoropropene, (Z)1-chloro-3,3,3-trifluoropropene or mixtures thereof. The resulting product stream includes (E)1-chloro-3,3,3-trifluoropropene and (Z)1-chloro-3,3,3-trifluoropropene, where the ratio of (E) isomer to (Z) isomer in the product stream is different than the ratio feed stream. The (E) and (Z) isomers in the product stream may be separated from one another.
1. A method of converting (E)1-chloro-3,3,3-trifluoropropene into (Z)1-chloro-3,3,3-trifluoropropene, comprising:
providing a feed stream consisting essentially of (E)1-chloro-3,3,3-trifluoropropene or a mixture of (E)1-chloro-3,3,3-trifluoropropene and (Z)1-chloro-3,3,3-trifluoropropene having less than about 5 wt % (Z)1-chloro-3,3,3-trifluoropropene;
contacting the feed stream with a heated surface that is maintained between 150° C. and 350° C. for a period of time sufficient to convert at least a portion of the (E)1-chloro-3,3,3-trifluoropropene to (Z)1-chloro-3,3,3-trifluoropropene to produce a product stream; and
distilling the product stream to separate the (E) and (Z) isomers from one another.
2. The method of claim 1 , further comprising the step of providing a temperature controlled reaction vessel that includes an interior surface, a first opening, a second opening, a pathway fluidly connecting the first and second openings, and a packing material disposed in the pathway, wherein the heated surface includes the interior surface and the packing material.
3. The method of claim 1 , wherein the feed stream has been vaporized before the step of contacting the feed stream with the heated surface.
4. The method of claim 1 , wherein the feed stream is vaporized after the step of contacting the feed stream with the heated surface.
5. The method of claim 1 , wherein sufficient (E)1-chloro-3,3,3-trifluoropropene is converted to (Z)1-chloro-3,3,3-trifluoropropene to yield a product stream having more than 5 wt % (Z)1-chloro-3,3,3-trifluoropropene.
6. The method of claim 1 , wherein the product stream has between about 5 wt % and about 17 wt % (Z)1-chloro-3,3,3-trifluoropropene.
7. The method of claim 1 , wherein the heated surface includes the outer surface of a packing material.
8. The method of claim 7 , wherein the packing material is a catalyst material.
9. The method of claim 8 , wherein the catalyst material is a metal oxide, halogenated metal oxide, a Lewis acid metal halide, or a zero-valent metal, or a mixture or alloy thereof.
10. The method of claim 8 , wherein the catalyst material is AlF 3 , fluorinated Cr 2 O 3 , or Cr 2 O 3 .
11. The method of claim 1 , wherein the product stream consists essentially of (E)1-chloro-3,3,3-trifluoropropene and (Z)1-chloro-3,3,3-trifluoropropene.
12. The method of claim 1 , wherein the method of converting is reagent-free.
13. A method of converting (Z)1-chloro-3,3,3-trifluoropropene into (E)1-chloro-3,3,3-trifluoropropene, comprising:
providing a feed stream consisting essentially of (Z)1-chloro-3,3,3-trifluoropropene or a mixture of (E)1-chloro-3,3,3-trifluoropropene and (Z)1-chloro-3,3,3-trifluoropropene having more than about 15 wt % (Z)1-chloro-3,3,3-trifluoropropene;
contacting the feed stream with a heated surface that is maintained between 50° C. and 350° C. for a period of time sufficient to convert at least a portion of the (Z)1-chloro-3,3,3-trifluoropropene to (E)1-chloro-3,3,3-trifluoropropene to produce a product stream; and
distilling the product stream to separate the (E)1-chloro-3,3,3-trifluoropropene and (Z)1-chloro-3,3,3-trifluoropropene from one another.
14. The method of claim 13 , wherein the amount of (E)1-chloro-3,3,3-trifluoropropene in the product stream is at least 5 percentage points higher than the wt % of (E)1-chloro-3,3,3-trifluoropropene in the feed stream.
15. The method of claim 13 , wherein the product stream has between about 5 wt % and about 50 wt % (Z)1-chloro-3,3,3-trifluoropropene.
16. The method of claim 13 , wherein the product stream has between about 50 wt % and about 95 wt % (E)1-chloro-3,3,3-trifluoropropene.
17. The method of claim 13 , further comprising the step of providing a temperature controlled reaction vessel that includes an interior surface, a first opening, a second opening, a pathway fluidly connecting the first and second openings, and a packing material disposed in the pathway, wherein the heated surface includes the interior surface and the packing material.
18. The method of claim 13 , wherein the feed stream has been vaporized before the step of feeding the feed stream into the reactor vessel.
19. The method of claim 13 , wherein the feed stream is vaporized after the step of feeding the feed stream into the reactor vessel.
20. The method of claim 13 , wherein the reactor vessel is packed with a packing material.
21. The method of claim 20 , wherein the packing material is a catalyst material.
22. The method of claim 21 , wherein the catalyst material is a metal oxide, a halogenated metal oxide, a Lewis acid metal halide, or a zero-valent metal, or a mixture or alloy thereof.
23. The method of claim 21 , wherein the catalyst material is AlF 3 , fluorinated Cr 2 O 3 , or Cr 2 O 3 .
24. The method of claim 13 , wherein the product stream consists essentially of (E)1-chloro-3,3,3-trifluoropropene and (Z)1-chloro-3,3,3-trifluoropropene.
25. The method of claim 13 , wherein the method of converting is reagent-free.