Processes for the production of fluoropropanes and halopropenes
US-RE49849-E · Feb 27, 2024 · US
US10577296B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10577296-B2 |
| Application number | US-201815917376-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 9, 2018 |
| Priority date | Mar 10, 2017 |
| Publication date | Mar 3, 2020 |
| Grant date | Mar 3, 2020 |
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The present application provides a process of preparing 3,3,3-trifluoroprop-1-ene, comprising reacting 3-chloro-1,1,1-trifluoropropane with a base in an aqueous solvent component in the absence of a phase transfer catalyst.
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What is claimed is: 1. A process of preparing 3,3,3-trifluoroprop-1-ene, comprising reacting 3-chloro-1,1,1-trifluoropropane with a base in an aqueous solvent component, wherein the reacting is conducted in the absence of a phase transfer catalyst, wherein the aqueous solvent component does not comprise an organic solvent. 2. The process of claim 1 , wherein the base is an aqueous base. 3. The process of claim 2 , wherein the base is a metal hydroxide base, a metal carbonate base, a metal phosphate base, or a metal fluoride base. 4. The process of claim 2 , wherein the base is NaOH, KOH, LiOH, CsOH, Ca(OH) 2 , Zn(OH) 2 , Na 2 CO 3 , K 2 CO 3 , K 3 PO 4 , Na 3 PO 4 , KF, or CsF. 5. The process of claim 2 , wherein the base is KOH or NaOH. 6. The process of claim 1 , wherein about 0.01 to about 5 molar equivalents of base is used based on one molar equivalent of 3-chloro-1,1,1-trifluoropropane. 7. The process of claim 1 , wherein the reacting is conducted at a temperature of from about 20 ° C. to about 100 ° C. 8. The process of claim 1 , wherein the reacting is conducted at a pressure of about −10 psig to about 500 psig. 9. The process of claim 1 , wherein the reacting comprises mixing the 3-chloro-1,1,1-trifluoropropane and base with a mixing power of from about 0.1 to about 50 horsepower per 1000 gallons of the reaction mixture. 10. The process of claim 1 , wherein the reacting is conducted at a temperature of from about 35 ° C. to about 80° C. and at a pressure of about 5 psig to about 230 psig. 11. The process of claim 1 , wherein the 3-chloro-1,1,1-trifluoropropane is prepared by a process comprising reacting 1,1,1,3-tetrachloropropane with hydrofluoric acid. 12. The process of claim 1 , further comprising chlorinating 3,3,3-trifluoropropene to form 1,1,1-trifluoro-2,3-dichloropropane (HCFC-243db). 13. The process of claim 12 , wherein said chlorinating comprises reacting with chlorine or HCl/oxygen. 14. The process of claim 12 , comprising dehydrochlorinating 1,1,1-trifluoro-2,3-dichloropropane (HCFC-243db) to form 2-chloro-3,3,3-trifluoropropene (HCFO-1233xf). 15. The process of claim 14 , comprising reacting the 1,1,1-trifluoro-2,3-dichloropropane (HCFC-243db) with caustic to form 2-chloro-3,3,3-trifluoropropene (HCFO-1233xf). 16. The process of claim 14 , further comprising hydrofluorinating 2-chloro-3,3,3,-trifluoropropene (HCFO-1233xf) with HF to form 2-chloro-1,1,1,2-tetrafluoropropane (HCFC-244bb). 17. The process of claim 14 , further comprising hydrofluorinating 2-chloro-3,3,3,-trifluoropropene (HCFO-1233xf) with HF to form 2,3,3,3-tetrafluoropropene (HFO-1234yf). 18. The process of claim 16 , further comprising dehydrochlorinating 2-chloro-1,1,1,2-tetrafluoropropane (HCFC-244bb) to form 2,3,3,3-tetrafluoropropene (HFO-1234yf). 19. The process of claim 16 , further comprising reacting 2-chloro-1,1,1,2-tetrafluoropropane (HCFC-244bb) with caustic to form 2,3,3,3-tetrafluoropropene (HFO-1234yf). 20. A process of preparing 3,3,3-trifluoroprop-1-ene comprising reacting 3-chloro-1,1,1-trifluoropropane with aqueous NaOH, wherein the reacting is performed at a temperature of from about 35 ° C. to about 80° C. and at a pressure of from about 5 psig to about 230 psig, and wherein the reacting is conducted in the absence of a phase transfer catalyst and an organic solvent component.
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