Process for geometric isomerization of halogenated olefins
View Patent ↗Disclosed are processes for the conversion of isomerizable halogenated C2-C6 olefins from one geometric form to a more preferred geometric form. Preferred process aspects comprise converting C2-C6 olefin in a cis-form to a trans-form comprising exposing the cis-form of the compound, preferably contained in process stream, to conditions effective to convert at least about 50 percent, and even more preferably at least about 70 percent, of the cis-form compound to the trans-form compound. Preferably the catalyst comprises at least one Lewis acid metal fluoride.
1. A process for the conversion of cis-1,3,3,3 tetrafluoropropene to trans-1,3,3,3 tetrafluoropropene comprising:
a) providing a reactor feed comprising cis-1,3,3,3 tetrafluoropropene; and
b) introducing said reactor feed to catalytic reaction conditions effective to convert at least a portion of said cis-1,3,3,3 tetrafluoropropene in said feed to trans-1,3,3,3 tetrafluoropropene, said conditions comprising exposing said feed, at a reaction temperature of from about 75 to about 350° C., to at least one Lewis acid metal fluoride.
2. The process of claim 1 wherein the metal component of said Lewis acid metal fluoride is selected from the group consisting of: (1) transition metals having an atomic number from about 21 to about 57; (2) metals from Group IIIA having an atomic number of from about 13 to about 81; (3) metals from Group VA having an atomic number of from about 51 to 83; (4) rare earth metals; (5) alkali metals from Group IA having an atomic number of from about 3 to about 37; (6) alkali metals from Group IIA having an atomic number of from about 12 to about 56; and (7) combinations of any two or more of them.
3. The process of claim 1 wherein the metal component of said Lewis acid metal fluoride is Al.
4. The process of claim 1 wherein the metal component of said Lewis acid metal fluoride is Fe.
5. The process of claim 1 wherein said reaction conditions are effective to convert at least about 5% of the cis-form and to achieve a selectivity to the trans-form of at least about 70%.
6. The process of claim 1 wherein said reactor feed comprises at least about 5% by weight of said cis-form.
7. The process of claim 1 wherein said reactor feed comprises at least about 5% by weight of said cis-form.
8. The process of claim 1 wherein said reactor feed is formed from at least a part of the effluent from one or more upstream reactions in a commercial process.
9. The process of claim 8 wherein said reactor feed comprises unreacted halogenated propanes and cis-form of fluorinated propenes.
10. The process of claim 1 wherein said reaction conditions are effective to convert at least about 70% of the cis-form and to achieve a selectivity to the trans-form of at least about 70%.
11. The process of claim 10 wherein said reaction conditions are effective to convert at least about 90% of the cis-form and to achieve a selectivity to the trans-form of at least about 80%.
12. The process of claim 10 wherein said reaction conditions are effective to convert at least about 95% of the cis-form and to achieve a selectivity to the trans-form of at least about 98%.
13. The process of claim 1 wherein said reaction temperature is from about 90 to about 250° C.
14. The process of claim 1 wherein said reaction temperature is about 200° C.
15. The process of claim 13 wherein said Lewis acid metal fluoride is aluminum fluoride.
16. The process of claim 14 wherein said Lewis acid metal fluoride is aluminum fluoride.
17. The process of claim 15 wherein said reaction conditions are effective to convert at least about 90% of the cis-form and to achieve a selectivity to the trans-form of at least about 80%.
18. The process of claim 15 wherein said reaction conditions are effective to convert at least about 95% of the cis-form and to achieve a selectivity to the trans-form of at least about 98%.
19. A process for the conversion of cis-1,3,3,3 tetrafluoro-propene to trans-1,3,3,3 tetrafluoropropene comprising:
a) providing a reactor feed comprising cis-1,3,3,3 tetrafluoropropene; and
b) introducing said reactor feed to catalytic reaction conditions effective to convert at least a portion of said cis-1,3,3,3 tetrafluoropropene in said feed to trans-1,3,3,3 tetrafluoropropene, said conditions comprising exposing said feed, at a reaction temperature of about 200° C., to aluminum fluoride.