Method for recovering anionic fluorinated emulsifier
View Patent ↗To provide a method for recovering an anionic fluorinated emulsifier, capable of easily and efficiently recovering an anionic fluorinated emulsifier adsorbed on a basic ion exchange resin. A basic ion exchange resin is brought into contact with a mixture of an aqueous inorganic acid solution and a non-aqueous fluorinated medium, or the basic ion exchange resin is brought into contact with an aqueous inorganic acid solution and then brought into contact with a non-aqueous fluorinated medium, then a phase of the non-aqueous fluorinated medium is recovered, and an acid of the anionic fluorinated emulsifier is recovered from the phase of the non-aqueous fluorinated medium.
1. A method for recovering an anionic fluorinated emulsifier, which comprises eluting, from a basic ion exchange resin on which an anionic fluorinated emulsifier is adsorbed, the anionic fluorinated emulsifier and recovering it as an acid of the anionic fluorinated emulsifier, wherein the basic ion exchange resin is brought into contact with a mixture of an aqueous inorganic acid solution and a non-aqueous fluorinated medium, a phase of the non-aqueous fluorinated medium is recovered, and the acid of the anionic fluorinated emulsifier is recovered from the phase of the non-aqueous fluorinated medium.
2. A method for recovering an anionic fluorinated emulsifier, which comprises eluting, from a basic ion exchange resin on which an anionic fluorinated emulsifier is adsorbed, the anionic fluorinated emulsifier and recovering it as an acid of the anionic fluorinated emulsifier, wherein the basic ion exchange resin is brought into contact with an aqueous inorganic acid solution and then brought into contact with a non-aqueous fluorinated medium, a phase of the non-aqueous fluorinated medium is recovered, and the acid of the anionic fluorinated emulsifier is recovered from the phase of the non-aqueous fluorinated medium.
3. The method for recovering an anionic fluorinated emulsifier according to claim 2 , wherein after the basic ion exchange resin is bought into contact with an aqueous inorganic acid solution, the basic ion exchange resin is separated and recovered, and then brought into contact with the non-aqueous fluorinated medium.
4. The method for recovering an anionic fluorinated emulsifier according to claim 1 , wherein the ratio of the aqueous inorganic acid solution and the non-aqueous fluorinated medium is such that the aqueous inorganic acid solution/the non-aqueous fluorinated medium=5/95 to 95/5 by the mass ratio.
5. The method for recovering an anionic fluorinated emulsifier according to claim 1 , wherein the ratio of the basic ion exchange resin, the aqueous inorganic acid solution and the non-aqueous fluorinated medium is such that the basic ion exchange resin/(total amount of the aqueous inorganic acid solution and the non-aqueous fluorinated medium)=60/40 to 1/99 by the mass ratio.
6. The method for recovering an anionic fluorinated emulsifier according to claim 1 , wherein the acid of the anionic fluorinated emulsifier is a fluorinated carboxylic acid.
7. The method for recovering an anionic fluorinated emulsifier according to claim 6 , wherein the acid of the anionic fluorinated emulsifier is a C 5-7 fluorinated carboxylic acid which may have one to three etheric oxygen atoms.
8. The method for recovering an anionic fluorinated emulsifier according to claim 1 , wherein the non-aqueous fluorinated medium is at least one member selected from the group consisting of a hydrofluorocarbon and a hydrofluoroether.
9. The method for recovering an anionic fluorinated emulsifier according to claim 8 , wherein the non-aqueous fluorinated medium is at least one member selected from the group consisting of CF 3 CH 2 OCF 2 CF 2 H, CF 3 CH 2 OCF 2 CFHCF 3 , (CF 3 ) 2 CHOCF 2 CF 2 H, CF 3 CH 2 OCHFCHF 2 , CF 3 (CF 2 ) 3 OCH 3 , CF 3 (CF 2 ) 4 OCH 3 , CF 3 (CF 2 ) 3 OCH 2 CH 3 , CF 3 (CF 2 ) 4 OCH 2 CH 3 , (CF 3 ) 2 CFCF 2 OCH 2 CH 3 , CHF 2 CF 2 CF 2 CF 2 CF 2 CF 3 , CF 3 CF 2 CF 2 CF 2 CH 2 CH 3 , CF 3 CF 2 CF 2 CF 2 CF 2 CF 2 CH 2 CH 3 , CF 3 CF 2 CHFCHFCF 3 , CF 3 CH 2 CF 2 CH 3 and CF 3 CF 2 CF 2 CFHCH 3 .
10. The method for recovering an anionic fluorinated emulsifier according to claim 1 , wherein the aqueous inorganic acid solution is at least one member selected from the group consisting of an aqueous hydrochloric acid solution, an aqueous sulfuric acid solution, an aqueous nitric acid solution and an aqueous phosphoric acid solution.
11. The method for recovering an anionic fluorinated emulsifier according to claim 1 , wherein the concentration of the aqueous inorganic acid solution is from 0.1N to 13N.
12. The method for recovering an anionic fluorinated emulsifier according to claim 1 , wherein the basic ion exchange resin is a strongly basic ion exchange resin.
13. The method for recovering an anionic fluorinated emulsifier according to claim 1 , wherein the rest after the phase of the non-aqueous fluorinated medium is separated, is brought into contact with the non-aqueous fluorinated medium, the phase of the non-aqueous fluorinated medium is separated and recovered, and the acid of the anionic fluorinated emulsifier is recovered from the phase of the non-aqueous fluorinated medium.
14. The method for recovering an anionic fluorinated emulsifier according to claim 3 , wherein the rest after the phase of the non-aqueous fluorinated medium is separated, is (A) brought into contact with a mixture of the aqueous inorganic acid solution and the non-aqueous fluorinated medium or (B) brought into contact with the aqueous inorganic acid solution, and then brought into contact with the non-aqueous fluorinated medium, the phase of the non-aqueous fluorinated medium is separated and recovered, and the acid of the anionic fluorinated emulsifier is recovered from the phase of the non-aqueous fluorinated medium.