PROCESS FOR PRODUCING FLUOROPROPENES

• US 20110015453A1
• Filed: 09/22/2010
• Published: 01/20/2011
• Est. Priority Date: 10/27/2003
• Status: Active Grant

• Current Assignee: Honeywell International Inc.
• Original Assignee: Honeywell International Inc.
• Inventors: Tung, Hsueh Sung, Merkel, Daniel C., Singh, Rajiv R.
• Granted Patent: US 8,034,984 B2
• Time in Patent Office: Days
• US Class Current: 570/156
• CPC Class Codes: C07C 17/206 the other compound being HX
• CPC Class Codes: C07C 17/25 by splitting-off hydrogen halides from halogenated hydrocarbons
• CPC Class Codes: C07C 19/08 containing fluorine
• CPC Class Codes: C07C 19/10 and chlorine
• CPC Class Codes: C07C 21/18 containing fluorine

Abstract

Dehydrohalogenation processes for the preparation of fluoropropenes from corresponding halopropanes, in which the fluoropropenes have the formula CF₃CY═CX_NH_P, wherein X and Y are independently hydrogen or a halogen selected from fluorine, chlorine, bromine and iodine; and N and P are independently integers equal to 0, 1 or 2, provided that (N+P)=2.

Claims

1. A process for the manufacture of 1,3,3,3-tetrafluoropropene comprising decomposing, in the presence of a fluorinated catalyst, a reactant comprising at least one of 1-chloro-1,3,3,3-tetrafluoropropane and 1,1,3,3,3-pentafluoropropane, under conditions sufficient to dehydrochlorinate 1-chloro-1,3,3,3-tetrafluoropropane and/or to dehydrofluorinate 1,1,1,3,3-pentafluoropropane, to form a reaction product which comprises 1,3,3,3-tetrafluoropropene.

2. The process of claim 1 wherein 1-chloro-1,3,3,3-tetrafluoropropane is dehydrochlorinated to form a reaction product which comprises 1,3,3,3-tetrafluoropropene.

3. The process of claim 1 wherein 1,1,3,3,3-pentafluoropropane is dehydrofluorinated to form a reaction product which comprises 1,3,3,3-tetrafluoropropene.

4. The process of claim 1 wherein said dehydrochlorination of 1-chloro-1,3,3,3-tetrafluoropropane and said dehydrofluorination of 1,1,1,3,3,-pentafluoropropane are conducted substantially simultaneously in the same reactor.

5. The process of claim 1 which is conducted at a temperature of from about 30°

C. to about 400°

C.

6. The process of claim 1 which is conducted at a temperature of from about 50°

C. to about 350°

C.

7. The process of claim 1 which is conducted at a temperature of from about 75°

C. to about 300°

C.

8. The process of claim 1 which is conducted at atmospheric pressure or under vacuum.

9. The process of claim 1 which is conducted a superatmospheric pressure.

10. The process of claim 1, wherein said fluorinated catalyst is a fluorinated transition metal oxide.

11. The process of claim 10 wherein said fluorinated transition metal oxide is fluorinated chromium (III) oxide.

12. The process of claim 11 wherein said fluorinated chromium (III) oxide is formed by fluorinating chromium (III) oxide with HF.

13. The process of claim 1 wherein the 1-chloro-1,3,3,3-tetrafluoropropane and/or 1,1,1,3,3-pentafluoropropane are previously prepared by fluorinating 1,1,1,3,3-pentachloropropane with hydrogen fluoride in the vapor phase in the presence of a fluorination catalyst.

14. The process of claim 13 wherein said fluorination catalyst is selected from the group consisting of transition metal halides, Group IVb metal halides, Group Vb metal halides and combinations thereof on activated carbon or fluorinated alumina.

15. The process of claim 13 wherein said fluorination catalyst is selected from the group consisting of SbCl₅, SbCl₃, SbF₅, TaCl₅, SnCl₄, NbCl₅, TiCl₄, MoCl₅, Cr₂O₃, Cr₂O₃/Al₂O₃, Cr₂O₃/AlF₃, Cr₂O₃/carbon, CoCl₂/Cr₂O₃/Al₂O₃, NiCl₂/Cr₂O₃/Al₂O₃, CoCl₂/AlF₃, NiCl₂/AlF₃ and combinations thereof.

16. The process of claim 13 wherein said fluorination catalyst is selected from the group consisting of Cr₂O₃, Cr₂O₃/carbon, Cr₂O₃/AlF₃, CoCl₂/AlF₃, NiCl₂/AlF₃ and combinations thereof.

17. The process of claim 13 wherein said fluorination catalyst comprises SbCl₃ or SbCl₅ supported on activated carbon.

18. The process of claim 13 wherein the fluorinating is conducted at a temperature of from about 100°

C. to about 350°

C.

19. The process of claim 13 wherein the fluorinating is conducted at atmospheric pressure or under vacuum.

20. The process of claim 13 wherein the fluorinating is conducted at superatmospheric pressure.

21. The process of claim 13 wherein the mole ratio of hydrogen fluoride to 1,1,1,3,3-pentachloropropane is from about 2:

1 to about 100;

1.

22. The process of claim 13 further comprising feeding chlorine to the fluorinating reaction to keep the fluorination catalyst active.

23. The process of claim 1 wherein the 1-chloro-1,3,3,3-tetrafluoropropane and/or 1,1,1,3,3-pentafluoropropane are previously prepared by fluorinating 1,1,1,3,3-pentachloropropane with hydrogen fluoride in a liquid phase in the presence of a fluorination catalyst.

24. The process of claim 23 wherein said fluorination catalyst is selected from the group consisting of transition metal halides, Group IVb metal halides, Group Vb metal halides and combinations thereof.

25. The process of claim 24 wherein said fluorination catalyst is selected from the group consisting of SbCl₅, SbCl₃, SbF₅, TaCl₅, SnCl₄, NbCl₅, TiCl₄, MoCl₅, and combinations thereof.

26. The process of claim 25 wherein said fluorination catalyst is selected from the group consisting of SbCl₅, SbCl₃ and combinations thereof.

27. The process of claim 23 wherein the fluorinating is conducted at a temperature of from about 60°

C. to about 180°

C.

28. The process of claim 23 wherein the fluorinating is conducted at a pressure of from about 50 psig and 400 psig.

29. The process of claim 23 wherein the mole ratio of hydrogen fluoride to 1,1,1,3,3-pentachloropropane is from about 2:

1 to about 100;

1.

30. The process of claim 23 further comprising feeding chlorine to the fluorinating reaction to keep the fluorination catalyst active.