Process for separating hydrogen fluoride from organic feedstocks
View Patent ↗Provided is a process for purifying an organic feedstock comprising (a) distilling a raw organic feedstock comprising hydrogen fluoride, 2-chloro-1,1,1,2-tetrafluoropropane, and 2-chloro-3,3,3-trifluoropropene to produce a first distillate stream comprising an azeotrope-like composition of 2-chloro-1,1,1,2-tetrafluoropropane, 2-chloro-3,3,3-trifluoropropene, and hydrogen fluoride, and a first bottoms stream rich in hydrogen fluoride; (b) cooling said first distillate stream to produce an intermediate composition comprising an organic layer rich in 2-chloro-1,1,1,2-tetrafluoropropane and 2-chloro-3,3,3-trifluoropropene, and an acid layer rich in hydrogen fluoride; and, optionally but preferably, (c) distilling said organic layer to produce a second distillate stream comprising an azeotrope-like composition of 2-chloro-1,1,1,2-tetrafluoropropane, 2-chloro-3,3,3-trifluoropropene, and hydrogen fluoride, and a second bottoms stream comprising a purified organic feedstock substantially free of hydrogen fluoride.
1. A process for purifying an organic feedstock comprising:
a. distilling a raw organic feedstock comprising hydrogen fluoride, 2-chloro-1,1,1,2-tetrafluoropropane, and 2-chloro-3,3,3-trifluoropropene to produce a first distillate stream comprising an azeotrope-like composition of 2-chloro-1,1,1,2-tetrafluoropropane, 2-chloro-3,3,3-trifluoropropene, and hydrogen fluoride, and a first bottoms stream rich in hydrogen fluoride; and
b. cooling said first distillate stream to a temperature between about −30° C. and about +10° C. to produce an intermediate composition comprising an organic layer rich in 2-chloro-1,1,1,2-tetrafluoropropane and 2-chloro-3,3,3-trifluoropropene, and an acid layer rich in hydrogen fluoride.
2. The method of claim 1 further comprising:
c. distilling said organic layer to produce a second distillate stream comprising an azeotrope-like composition of 2-chloro-1,1,1,2-tetrafluoropropane, 2-chloro-3,3,3-trifluoropropene, and hydrogen fluoride, and a second bottoms stream comprising a purified organic feedstock substantially free of hydrogen fluoride.
3. The process of claim 1 wherein said raw organic feedstock comprises about 60 to about 70 weight percent hydrogen fluoride.
4. The process of claim 1 wherein said first distillate stream comprises about 20 to about 30 weight percent hydrogen fluoride.
5. The process of claim 1 wherein said cooling produces a first distillate stream having a temperature of about −30° C. to about −10° C.
6. The process of claim 1 wherein said organic layer comprises less than about 5 weight percent hydrogen fluoride.
7. The process of claim 1 wherein said organic layer is separated from said acid layer prior to step (c).
8. The process of claim 2 wherein said second bottoms stream comprises at least about 80 weight percent of the combined mass of said 2-chloro-1,1,1,2-tetrafluoropropane and 2-chloro-3,3,3-trifluoropropene in said raw organic feedstock.