Dehydrohalogenation of hydrochlorofluorocarbons
US-10927061-B2 · Feb 23, 2021 · US
US12247000B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12247000-B2 |
| Application number | US-202318479882-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 3, 2023 |
| Priority date | Sep 11, 2015 |
| Publication date | Mar 11, 2025 |
| Grant date | Mar 11, 2025 |
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A dehydrohalogenation product includes a hydrochlorofluorocarbon mixture of a fluoroolefin of formula RCX=CZQ and a halofluoroalkane of formula RCXYCZQT. R is a perfluorinated alkyl group and X, Z, and Q are independently H or halogen. One of Y and T is H and the other is Cl, Br, or I. About 80% or greater of the hydrochlorofluorocarbon mixture is the fluoroolefin. The dehydrohalogenation product also includes a caustic agent and a solvent. In some embodiments, the dehydrohalogenation product is free of any catalyst, including any phase transfer catalyst.
Opening claim text (preview).
What is claimed is: 1. A dehydrochlorination process comprising vigorously contacting a chlorofluoroalkane of formula RCXYCZQT in an aqueous solvent comprising NaOH in a molar ratio of about 0.5 to about 2.0 of NaOH:chlorofluoroalkane, in the absence of any additional phase transfer catalyst, at a temperature in the range of about 30° C. to about 80° C. to produce a product comprising a fluoroolefin of formula RCX=CZQ, wherein R is a perfluorinated alkyl group and X, Z, and Q are independently H or fluorine, and one of Y and T is H and the other is Cl, wherein the conversion by the dehydrochlorination process is at least 95% of the maximum based on a starting ratio of NaOH and chlorofluoroalkane. 2. The dehydrochlorination process of claim 1 , wherein the conversion by the dehydrochlorination process is at least 98% of the maximum based on the starting ratio of NaOH and chlorofluoroalkane. 3. The dehydrochlorination process of claim 1 , wherein RCX=CZQ comprises one of CF 3 CF═CH 2 , CF 3 CH═CHF, and CF 3 CCl═CH 2 . 4. The dehydrochlorination process of claim 3 , wherein RCX=CZQ comprises CF 3 CF═CH 2 . 5. The dehydrochlorination process of claim 1 , wherein the aqueous solvent further comprises a co-solvent. 6. The dehydrochlorination process of claim 1 , wherein the dehydrohalogenation is conducted for about 1 to 120 minutes. 7. The dehydrochlorination process of claim 6 , wherein the dehydrohalogenation is conducted for about 10 to about 45 minutes. 8. The dehydrochlorination process of claim 1 , wherein the fluoroolefin is a chlorofluoroolefin. 9. The process of claim 1 , wherein the vigorous contacting involves agitation. 10. The process of claim 1 , wherein the vigorous contacting involves a mixing power at a horsepower in the range of 0.5 to 40 per 1000 gallons. 11. The process of claim 10 , wherein the mixing power is at a horsepower in the range of 1.2 to 40 per 1000 gallons. 12. The process of claim 1 , wherein the temperature is in the range of about 50 to about 80° C. 13. The process of claim 1 , wherein the aqueous solvent is about 12 wt % NaOH. 14. The process of claim 1 , wherein the molar ratio of NaOH:chlorofluoroalkane is sufficient to convert at least 99% of the chlorofluoroalkane. 15. A composition comprising: a hydrochlorofluorocarbon mixture comprising: a fluoroolefin of formula RCX=CZQ, wherein R is a perfluorinated alkyl group and X, Z, and Q are independently H or fluorine; and a chlorofluoroalkane of formula RCXYCZQT, wherein one of Y and T is H and the other is Cl; and an aqueous solvent comprising NaOH in a molar ratio of 0.5 to 2.0 of NaOH:hydrochlorofluorocarbon mixture. 16. The composition of claim 15 , wherein RCX=CZQ comprises one of CF 3 CF═CH 2 , CF 3 CH═CHF, and CF 3 CCl═CH 2 . 17. The composition of claim 16 , wherein RCX=CZQ comprises CF 3 CF═CH 2 . 18. The composition of claim 15 , the aqueous solvent further comprising a co-solvent. 19. The composition of claim 15 , wherein the NaOH is about 12 wt % in aqueous solvent. 20. The composition of claim 15 , wherein the composition is free of any additional phase transfer catalyst and wherein the molar ratio of NaOH:chlorofluoroalkane is sufficient to convert at least 95% of the chlorofluoroalkane based on a starting ratio of NaOH and chlorofluoroalkane.
of halogen atoms by other halogen atoms · CPC title
containing fluorine · CPC title
Halogenated hydrocarbons · CPC title
Unsaturated fluorinated hydrocarbons · CPC title
Foams · CPC title
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