Method for recovering trans-1,2-dichloroethene
View Patent ↗Describes a method for recovering trans-1,2-dichloroethene from a liquid feed composition comprising both the cis-and trans-isomers of 1,2-dichloroethene and contaminating amounts of other chlorinated hydrocarbons, e.g., lower alkyl chlorinated hydrocarbons, such as C 1- C 2 chlorinated hydrocarbons. In one of the described methods, the liquid feed composition is introduced into a first distillation column 10 wherein the stereoisomers and chlorinated hydrocarbons more volatile than the stereoisomers are removed as overhead 12 and charged to a second distillation column 20 . In column 20 , the stereoisomers are separated from the more volatile chlorinated hydrocarbons, and a bottoms fraction 24 comprising the stereoisomers is charged to a reactive distillation column 30 wherein the cis-isomer is isomerized to the trans-isomer in the liquid phase and in the presence of an organic free-radical initiator, e.g., an azonitrile initiator. Substantially pure trans 1,2-dichloroethene is recovered as overhead 32 from reactive distillation column 30.
1. A method for recovering trans-1,2-dichloroethene from a liquid composition comprising the stereoisomers trans-1,2-dichloroethene and cis-1,2-dichloroethene, and contaminating amounts of other chlorinated hydrocarbons, comprising:
(a) distilling said liquid composition in a first distillation zone;
(b) removing first distillate comprising said stereoisomers trans-1,2-dichloroethene and cis-1,2-dichloroethene, and chlorinated hydrocarbons having a lower boiling temperature than said stereoisomers from said first distillation zone;
(c) distilling at least a portion of the first distillate in a second distillation zone, and removing a liquid stream comprising said stereoisomers from the second distillation zone;
(d) introducing at least a portion of the liquid stream comprising said stereoisomers removed from the second distillation zone into a reactive distillation zone containing organic free-radical initiator;
(e) isomerizing cis-1,2-dichloroethene to trans-1,2-dichloroethene in said reactive distillation zone; and
(f) recovering substantially pure trans-1,2-dichloroethene product from said reactive distillation zone.
2. The method of claim 1 wherein the contaminating amount of other chlorinated hydrocarbons comprise at least 20 weight percent of the liquid composition.
3. The method of claim 1 wherein the contaminating amount of other chlorinated hydrocarbons comprise from 20 to 80 weight percent of the liquid composition.
4. The method of claim 1 wherein the other chlorinated hydrocarbons comprise C 1 -C 2 chlorinated hydrocarbons.
5. The method of claim 4 wherein the other chlorinated hydrocarbons comprise from 30 to 70 weight percent of the liquid composition.
6. The method of claim 4 wherein the chlorinated hydrocarbons are chosen from chloroform, methylene chloride, carbon tetrachloride, vinylidene chloride, vinyl chloride, trichioroethane, trichloroethylene, ethyl chloride, ethylene dichloride, perchloroethylene, pentachloroethane and mixtures of at least two of said chlorinated hydrocarbons.
7. The method of claim 1 wherein the free-radical initiator is an organic azonitrile initiator.
8. The method of claim 1 wherein the free-radical initiator is present in the reactive distillation zone in amounts of from 5 to 5000 ppm.
9. The method of claim 1 wherein the free-radical initiator is present in the reactive distillation zone in amounts of from 100 to 2000 ppm.
10. The method of claim 7 wherein the initiator is azobisisobutyronitrile.
11. The method of claim 10 wherein the azobisisobutyronitrile is present in amounts of from 25 to 1000 ppm.
12. The method of claim 10 wherein the temperature at which the cis-isomer is isomerized to the trans-isomer is from 190° F. to 235° F.
13. A method for recovering trans-1,2-dichloroethene from a liquid composition comprising the stereoisomers trans-1,2-dichloroethene and cis-1,2-dichloroethene, and from 35 to 65 weight percent of other chlorinated hydrocarbons, comprising:
(a) distilling said liquid composition in a first distillation zone;
(b) removing first distillate comprising said stereoisomers trans-1,2-dichloroethene and cis-1,2-dichloroethene, and chlorinated hydrocarbons having a lower boiling temperature than said stereoisomers from said first distillation zone;
(c) distilling at least a portion of the first distillate in a second distillation zone, and removing a liquid stream comprising said stereoisomers from the second distillation zone;
(d) introducing at least a portion of the liquid stream comprising said stereoisomers removed from the second distillation zone into a reactive distillation zone containing organic free-radical initiator;
(e) isomerizing cis-1,2-dichloroethene to trans-1,2-dichloroethene in the liquid phase in said reactive distillation zone; and
(f) recovering substantially pure trans-1,2-dichloroethene product from said reactive distillation zone.
14. The method of claim 13 wherein the other chlorinated hydrocarbons comprise C 1 -C 2 chlorinated hydrocarbons.
15. The method of claim 14 wherein the chlorinated hydrocarbons are chosen from chloroform, methylene chloride, carbon tetrachloride, vinylidene chloride, vinyl chloride, trichloroethane, trichloroethylene, ethyl chloride, ethylene dichloride, perchloroethylene, pentachloroethane and mixtures of at least two of said chlorinated hydrocarbons.
16. The method of claim 13 wherein the free-radical initiator is an organic azonitrile initiator that is present in the reactive distillation zone in amounts of from 5 to 2000 ppm.
17. The method of claim 16 wherein the free-radical initiator is azobisisobutyronitrile, which is present in amounts of from 25 to 1000 ppm.
18. The method of claim 17 wherein the temperature at which the cis-isomer is isomerized to the trans-isomer is from 190° F. to 235° F.
19. A method for recovering trans-1,2-dichloroethene from a liquid composition comprising the cis- and trans- stereoisomers of 1,2-dichloroethene and contaminating amounts of other chlorinated hydrocarbons, comprising:
(a) separating the cis- and trans- stereoisomers of 1,2-dichloroethene and chlorinated hydrocarbons more volatile than said stereoisomers as a first fraction from said liquid composition in a first separation zone;
(b) introducing at least a portion of the first fraction removed from the first separation zone into a second separation zone, and removing as a second fraction from the second separation zone chlorinated hydrocarbons more volatile than said stereoisomers of 1,2-dichloroethene;
(c) removing a third fraction comprising the cis- and trans- stereoisomers of 1,2-dichloroethene from the second separation zone;
(d) introducing at least a portion of the third fraction comprising the cis- and trans- stereoisomers of 1,2-dichloroethene removed from the second separation zone into a reaction zone;
(e) isomerizing cis-1,2-dichloroethene to trans-1,2-dichloroethene within said reaction zone, said isomerization being conducted in the liquid phase and in the presence of an organic free-radical initiator; and
(f) recovering substantially pure trans-1,2-dichloroethene product from said reaction zone.
20. The method of claim 19 wherein the other chlorinated hydrocarbons comprise C 1 -C 2 chlorinated hydrocarbons and are present in the liquid composition in amounts of from 20 to 80 weight percent.
21. The method of claim 20 wherein the other chlorinated hydrocarbons are chosen from chloroform, methylene chloride, methyl chloroform, carbon tetrachloride, vinylidene chloride, vinyl chloride, trichloroethane, trichloroethylene, ethyl chloride, ethylene dichloride, perchloroethylene, pentachloroethane and mixtures of at least two of said chlorinated hydrocarbons.
22. The method of claim 21 wherein the free-radical initiator is an organic azonitrile initiator, which is present in the reactive distillation zone in amounts of from 5 to 2000 ppm.
23. The method of claim 22 wherein the azonitrile initiator is azobisisobutyronitrile, which is present in amounts of from 25 to 1000 ppm.
24. A method for recovering trans-1,2-dichloroethene from a liquid composition comprising the stereoisomers trans-1,2-dichloroethene and cis-1,2-dichloroethene, and contaminating amounts of other chlorinated hydrocarbons, comprising:
(a) distilling said liquid composition in a first distillation zone;
(b) separating in said first distillation zone chlorinated hydrocarbons more volatile than the stereoisomers trans-1,2-dichloroethene and cis-1,2-dichloroethene from the liquid composition, thereby to produce a second liquid composition comprising said stereoisomers;
(c) distilling at least a portion of said second liquid composition in a second distillation zone, and removing an overhead stream comprising principally trans-1,2-dichloroethene and cis-1,2-dichloroethene from said second distillation zone;
(d) introducing at least a portion of the overhead stream from the second distillation zone into a reactive distillation zone containing organic free-radical initiator;
(e) isomerizing cis-1,2-dichloroethene to trans-1,2-dichloroethene in said reactive distillation zone; and
(f) recovering substantially pure trans-1,2-dichloroethene product from said reactive distillation zone.
25. The method of claim 24 wherein the contaminating amount of other chlorinated hydrocarbons comprise from 20 to 80 weight percent of the liquid composition.
26. The method of claim 25 wherein the other chlorinated hydrocarbons comprise C 1 -C 2 chlorinated hydrocarbons.
27. The method of claim 26 wherein the chlorinated hydrocarbons are chosen from chloroform, methylene chloride, carbon tetrachloride, vinylidene chloride, vinyl chloride, trichioroethane, trichloroethylene, ethyl chloride, ethylene dichloride, perchloroethylene, pentachloroethane and mixtures of at least two of said chlorinated hydrocarbons.
28. The method of claim 24 wherein the free-radical initiator is an organic azonitrile initiator.
29. The method of claim 24 wherein the free-radical initiator is present in the reaction distillation zone in amounts of from 100 to 2000 ppm.
30. The method of claim 28 wherein the free-radical initiator is azobisisobutyronitrile.
31. The method of claim 30 wherein the azobisisobutyronitrile is present in the reactive distillation zone in amounts of from 25 to 1000 ppm.
32. The method of claim 30 wherein the temperature at which the cis-isomer is isomerized to the trans-isomer is from 190° F. to 235° F.
33. A method for recovering trans-1,2-dichloroethene from a liquid composition comprising the stereoisomers trans-1,2-dichloroethene and cis-1,2-dichloroethene, and contaminating amounts of other chlorinated hydrocarbons, comprising:
(a) fractionally distilling said liquid composition in a first distillation zone;
(b) removing first distillate comprising said stereoisomers trans-1,2-dichloroethene and cis-1,2-dichloroethene, and chlorinated hydrocarbons having a lower boiling temperature than said stereoisomers from said first distillation zone;
(c) fractionally distilling at least a portion of the first distillate in a second distillation zone, and removing a liquid fraction comprising principally said stereoisomers from the second distillation zone;
(d) introducing at least a portion of the liquid fraction comprising said stereoisomers removed from the second distillation zone into a reactive distillation zone containing organic free-radical initiator;
(e) isomerizing cis-1,2-dichloroethene to trans-1,2-dichloroethene in the liquid phase in said reactive distillation zone; and
(f) recovering substantially pure trans-1,2-dichloroethene product from said reactive distillation zone.
34. The method of claim 33 wherein the contaminating amount of other chlorinated hydrocarbons comprise at least 20 weight percent of the liquid composition and further comprise C 1 -C 2 chlorinated hydrocarbons chosen from chloroform, methylene chloride, carbon tetrachloride, vinylidene chloride, vinyl chloride, trichloroethane, trichloroethylene, ethyl chloride, ethylene dichloride, perchloroethylene, pentachloroethane and mixtures of at least two of said chlorinated hydrocarbons.
35. The method of claim 34 wherein the organic free-radical initiator is an organic azonitrile initiator that is present in the reactive distillation zone in amounts of from 100 to 2000 ppm.
36. The method of claim 35 wherein the organic azonitrile initiator is azobisisobutyronitrile.
37. A method for recovering trans-1,2-dichloroethene from a liquid composition comprising the stereoisomers trans-1,2-dichloroethene and cis-1,2-dichloroethene, and contaminating amounts of other chlorinated hydrocarbons, comprising:
(a) distilling said liquid composition in a first distillation zone;
(b) recovering from said first distillation zone a composition comprising said stereoisomers trans-1,2-dichloroethene and cis-1,2-dichloroethene as either:
(1) an overhead stream comprising said stereoisomers and chlorinated hydrocarbons having a lower boiling temperature than said stereoisomers, or
(2) a liquid stream comprising said stereoisomers and chlorinated hydrocarbons having a higher boiling temperature than said stereoisomers;
(c) distilling at least a portion of said composition recovered from the first distillation zone in a second distillation zone;
(d) recovering from said second distillation zone a composition comprising principally trans-1,2-dichloroethene and cis-1,2-dichloroethene, and introducing at least a portion of said recovered composition into a reactive distillation zone containing organic free-radical initiator;
(e) isomerizing cis-1,2-dichloroethene to trans-1,2-dichloroethene in said reactive distillation zone; and
(f) recovering substantially pure trans-1,2-dichloroethene product from said reactive distillation zone.
38. The method of claim 37 wherein the contaminating amount of other chlorinated hydrocarbons comprise at least 20 weight percent of the liquid composition and further comprise C 1 -C 2 chlorinated hydrocarbons chosen from chloroform, methylene chloride, carbon tetrachloride, vinylidene chloride, vinyl chloride, trichioroethane, trichloroethylene, ethyl chloride, ethylene dichloride, perchloroethylene, pentachloroethane and mixtures of at least two of said chlorinated hydrocarbons.
39. The method of claim 38 wherein the organic free-radical initiator is an organic azonitrile initiator that is present in the reactive distillation zone in amounts of from 100 to 2000 ppm.
40. The method of claim 39 wherein the organic azonitrile initiator is azobisisobutyronitrile.
41. The method of claim 40 wherein the azobisisobutyronitrile is present in amounts of from 25 to 1000 ppm, and the temperature at which the cis-isomer is isomerized to the trans-isomer is from 190° F. to 235° F.