Process for producing perfluoropolymer, production apparatus and process for producing electrolyte membrane for polymer electrolyte fuel cells
View Patent ↗A process for producing a perfluoropolymer, the process including extruding a polymer obtained by polymerizing a perfluoromonomer to prepare strands, and bringing a gas comprising from 3 to 50 volume % of fluorine gas into contact with the strands; the process being conducted on an apparatus that includes an extruder for melting and extruding the polymer obtained by polymerizing a perfluoromonomer, a die having a plurality of pores for preparing the strands from the molten polymer extruded, and a fluorination tank for bringing the gas comprising from 3 to 50 volume % of fluorine gas into contact with the strands.
1. A process for producing a perfluoropolymer with reduced chain terminal unstable functional groups, which comprises
extruding a polymer comprising chain terminal unstable functional groups, obtained by polymerizing a perfluoromonomer, to prepare polymer strands comprising chain terminal unstable functional groups, and
reducing the polymer strands chain terminal unstable functional groups by bringing a gas comprising from 3 to 50 volume % of fluorine gas into contact with the polymer strands in a molten state such that fluorine gas is absorbed and diffused into the polymer strands and is reacted with chain terminal unstable terminal groups throughout the polymer strands, thereby reducing the chain terminal unstable functional groups throughout the polymer strands.
2. The process for producing a perfluoropolymer according to claim 1 , wherein the gas is brought into contact with the polymer strands at a temperature of from 150 to 350° C.
3. The process for producing a perfluoropolymer according to claim 1 , wherein the polymer has —SO 2 F groups.
4. The process for producing a perfluoropolymer according to claim 3 , wherein the polymer is a copolymer of tetrafluoroethylene and a compound represented by the following formula (I):
CF 2 ═CF(OCF 2 CFX) p (O) q (CF 2 ) n SO 2 F (1)
wherein X is a fluorine atom or a trifluoromethyl group, p is an integer of from 0 to 8, q is 0 or 1, n is an integer of from 0 to 8, and p+n>0.
5. The process of claim 4 , wherein the compound of formula (1) is a compound having the formula (I-1):
CF 2 ═CFO(CF 2 ) r SO 2 F (1-1),
wherein r is an integer ranging from 1 to 9.
6. The process of claim 5 , wherein r is 1.
7. The process of claim 5 , wherein r is 2.
8. The process of claim 4 , wherein the compound of formula (I) is a compound having the formula (I-2):
CF 2 ═CFOCF 2 CF(CF 3 )O(CF 2 ) 5 SO 2 F (1-2),
wherein s is an integer ranging from 1 to 8.
9. The process of claim 4 , wherein the compound of formula (1) is a compound of formula (I-3):
CF 2 ═CF(CF 2 ) t SO 2 F (1-3),
wherein t is an integer ranging from 0 to 8.
10. The process of claim 4 , wherein the compound of formula (1) is a compound of formula (I-4):
CF 2 ═CF[OCF 2 CF(CF 3 )] z O(CF 2 ) 2 SO 2 F (1-4),
wherein z is 2 or 3.
11. The process for producing a perfluoropolymer according to claim 3 , wherein the gas is brought into contact with the polymer strands at a temperature of from 150 to 350° C.
12. The process for producing a perfluoropolymer according to claim 11 , wherein the polymer is a copolymer of tetrafluoroethylene and a compound represented by the following formula (1):
CF 2 ═CF(OCF 2 CFX) p (O) q (CF 2 ) n SO 2 F (1)
wherein X is a fluorine atom or a trifluoromethyl group, p is an integer of from 0 to 8, q is 0 or 1, n is an integer of from 0 to 8, and p+n>0.
13. The process of claim 1 , wherein the chain terminal unstable functional groups comprise —COOH groups.
14. The process of claim 1 , wherein the chain terminal unstable functional groups comprise —CF═CF 2 groups.
15. The process of claim 1 , wherein the chain terminal unstable functional groups comprise —COF groups.
16. The process of claim 1 , wherein the chain terminal unstable functional groups comprise —CF 2 H groups.
17. The process of claim 1 , wherein the diameter of the pores in the die is from 0.5 to 5 mm.
18. The process of claim 1 , wherein the diameter of the pores in the die is from 1 to 3 mm.
19. The process of claim 1 , wherein the polymer strands are supplied to the fluorination tank continuously and the contacting of the polymer strands with the fluorine-containing gas is carried out continuously.
20. The process according to claim 1 , wherein said process is conducted in an apparatus comprising
an extruder for melting and extruding the polymer obtained by polymerizing the perfluoromonomer,
a die having a plurality of pores for preparing the polymer strands from the molten polymer extruded, and
a fluorination tank for bringing the gas comprising from 3 to 50 volume % of fluorine gas into contact with the polymer strands.