Process and methods of purification for the manufacture fluorocarbons
View Patent ↗Halocarbons of the structure CF 3 CF 2 CH 2 X, wherein X is either F or Cl or mixtures thereof prepared by: contacting at least one 2-fluorochloropropane with hydrogen fluoride in a first fluorination step in the gas phase or liquid phase under substantially anhydrous conditions, in the absence of added catalyst to partially fluorinate said 2-fluorochloropropane; contacting said partially fluorinated 2-fluorochloropropane with at least the stoichiometric molar equivalent of hydrogen fluoride under substantially anhydrous conditions, in the presence of at least one fluorination catalyst in a second fluorination step; removing said reaction products from contact with said catalyst, and isolating a substantial yield of at least 1,1,1,2,2,3-hexafluoropropane or 1,1,1,2,2,penta-3-chloropropane, or mixtures thereof, respectively.
1. An azeotropic composition comprising about 44.9 mole percent to about 63.1 mole percent 1,1,1,2,2,3-hexafluoropropane and about 36.9 mole percent to about 55.1 mole percent HF.
2. The azeotropic composition of claim 1 wherein the composition has a boiling point between about −6.1° C. and 108° C. at a pressure from between about 15 psi and 490 psia.
3. A near-azeotropic composition comprising about 38 mole percent to about 75.8 mole percent 1,1,1,2,2,3-hexafluoropropane and about 24.2 mole percent to about 62 mole percent HF.
4. An azeotropic composition consisting essentially of about 44.9 mole percent to about 63.1 mole percent 1,1,1,2,2,3-hexafluoropropane and about 36.9 mole percent to about 55.1 mole percent HF.
5. The azeotropic composition of claim 4 wherein the composition has a boiling point between about −6.1° C. and 108° C. at a pressure from between about 15 psi and 490 psia.
6. A near-azeotropic composition consisting essentially of about 38 mole percent to about 75.8 mole percent 1,1,1,2,2,3-hexafluoropropane and about 24.2 mole percent to about 62 mole percent HF.