Process for preparing fluorocarboxylic acids
View Patent ↗A fluorocarboxylic acid preparation process which includes hydrolyzing fluorocarboxylic acid fluoride in the presence of an aqueous sulfuric acid solution to form a reaction product containing a fluorocarboxylic acid and hydrogen fluoride (present as hydrofluoric acid); and removing at least some of the hydrogen fluoride from the reaction product by washing the reaction production with aqueous sulfuric acid solution. The hydrolyzing and washing are carried out at a temperature at which the fluorocarboxylic acid is a liquid.
1. A process for preparing fluorocarboxylic acid, which comprises:
hydrolyzing a fluorocarboxylic acid fluoride in the presence of an aqueous sulfuric acid solution to form a reaction product containing a fluorocarboxylic acid and hydrogen fluoride; and
removing at least some of the hydrogen fluoride from the reaction product by washing the reaction product with an aqueous sulfuric acid solution,
wherein said hydrolyzing and said washing are carried out at a temperature at which said fluorocarboxylic acid is a liquid.
2. The process of claim 1 , wherein the fluorocarboxylic acid fluoride has the general formula
X—RfCOF
in which X is a hydrogen atom, a fluorine atom or a chlorine atom, and Rf is a linear or branched fluoroalkyl group of 4 to 14 carbons.
3. The process of claim 2 , wherein the fluorocarboxylic acid fluoride has the general formula
X—(CF 2 ) m —O—(CF(CF 3 )CF 2 O) n —CF(CF 3 )COF
in which X is a hydrogen atom, a fluorine atom or a chlorine atom, m is an integer from 1 to 10, and n is an integer from 0 to 5.
4. The process of claim 1 , which comprises hydrolyzing said fluorocarboxylic acid fluoride in a liquid-liquid heterophase dispersed system including an aqueous phase and an organic phase, and maintaining the aqueous phase at a sulfuric acid concentration of about 5 to 50 wt %.
5. The process of claim 1 , which comprises washing the reaction product with a liquid-liquid heterophase dispersed system including an aqueous phase and an organic phase, and maintaining the aqueous phase at a sulfuric acid concentration of about 5 to 50 wt %.
6. The process of claim 4 , wherein hydrolysis is carried out continuously by countercurrent contact between the organic phase and the aqueous phase.
7. The process of claim 5 , wherein washing is carried out continuously by countercurrent contact between the organic phase and the aqueous phase.
8. The process of claim 1 , which comprises hydrolyzing said fluorocarboxylic acid fluoride and washing the reaction product both in a liquid-liquid heterophase dispersed system including an aqueous phase and an organic phase, and maintaining the aqueous phase at a sulfuric acid concentration of about 5 to 50 wt %, wherein hydrolysis and washing are carried out continuously by countercurrent contact between the organic phase and the aqueous phase in a single apparatus.
9. The process of claim 8 , wherein said apparatus comprises a differential contacting extraction tower.
10. The process of claim 1 , wherein the fluorocarboxylic acid fluoride comprises C 7 F 15 COF.
11. The process of claim 1 , wherein said hydrolysis and washing are carried out batchwise.
12. A process for purifying a reaction product containing a fluorocarboxylic acid and hydrogen fluoride as a by-product, which comprises:
washing the reaction product with an aqueous sulfuric acid solution to remove at least some of the hydrogen fluoride.
13. The process of claim 12 , which comprises washing the reaction product with a liquid-liquid heterophase dispersed system including an aqueous phase and an organic phase, and maintaining the aqueous phase at a sulfuric acid concentration of about 5 to 50 wt %.
14. The process of claim 13 , wherein washing is carried out continuously by countercurrent contact between the organic phase and the aqueous phase.
15. The process of claim 12 , wherein said washing is carried out batchwise.
16. A process for preparing fluorocarboxylic acid, which comprises:
hydrolyzing a fluorocarboxylic acid fluoride in the presence of an aqueous sulfuric acid solution to form a reaction product containing a fluorocarboxylic acid and hydrogen fluoride.
17. The process of claim 16 , wherein the fluorocarboxylic acid fluoride has the general formula
X—RfCOF
in which X is a hydrogen atom, a fluorine atom or a chlorine atom, and Rf is a linear or branched fluoroalkyl group of 4 to 14 carbons.
18. The process of claim 17 , wherein the fluorocarboxylic acid fluoride has the general formula
X—(CF 2 ) m —O—(CF(CF 3 )CF 2 O) n —CF(CF 3 )COF
in which X is a hydrogen atom, a fluorine atom or a chlorine atom, m is an integer from 1 to 10, and n is an integer from 0 to 5.
19. The process of claim 16 , which comprises hydrolyzing said fluorocarboxylic acid fluoride in a liquid-liquid heterophase dispersed system including an aqueous phase and an organic phase, and maintaining the aqueous phase at a sulfuric acid concentration of about 5 to 50 wt %.
20. The process of claim 19 , wherein hydrolysis is carried out continuously by countercurrent contact between the organic phase and the aqueous phase.
21. The process of claim 16 , wherein the fluorocarboxylic acid fluoride comprises C 7 F 15 COF.
22. The process of claim 16 , wherein said hydrolysis is carried out batchwise.