Method for producing fluororesin film
To provide a method for producing a fluororesin film, whereby defects due to deterioration (such as fish-eyes due to gelation) of a melt-processable fluororesin are less likely to occur during the production. A method for producing a fluororesin film, which comprises extruding a fluororesin material containing a melt-processable fluororesin through an extruder die, wherein the temperature of the extruder die is from 305 to 355° C., and the average flow velocity v 0.95 of the fluororesin material as obtained by v 0.95 =Q 0.95 /A 0.95 , is at least 1×10 −4 m/sec. Here, when the distance from the flow inlet 22 of the extruder die to the end of the manifold 24 of the extruder die is set to be x=1, Q 0.95 is the flow rate (m 3 /sec) of the fluororesin material flowing in the manifold 24 at a position of x=0.95 from the flow inlet 22 , and A 0.95 is the cross-sectional area (m 2 ) of the manifold 24 at a position of x=0.95 from the flow inlet 22.
1. A method for producing a fluororesin film, comprising extruding a fluororesin material comprising a melt-processable fluororesin through an extrusion die, wherein
the temperature of the extrusion die is from 305 to 355° C., and
the average flow velocity v 0.95 of the fluororesin material as obtained by formula (1) is at least 6.58×10 −4 m/sec.:
v 0.95 =Q 0.95 /A 0.95 (1)
wherein when a distance x from a flow inlet of the extrusion die to an end portion of a manifold of the extrusion die, is set to be 1,
Q 0.95 is a flow rate (m 3 /sec.) of the fluororesin material flowing in the manifold at a position of x=0.95 from the flow inlet, and
A 0.95 is a cross-sectional area (m 2 ) of the manifold at a position of x=0.95 from the flow inlet.
2. The method for producing a fluororesin film according to claim 1 , wherein a melt flow rate of the fluororesin at the temperature of the extrusion die and at a load of 49N, is at least 7 g/10 min.
3. The method for producing a fluororesin film according to claim 1 , wherein a width of a lip opening of the extrusion die is from 0.5 to 3.0 mm.
4. The method for producing a fluororesin film according to claim 1 , wherein the fluororesin is a copolymer having units derived from tetrafluoroethylene, units derived from a monomer having an adhesive functional group, and units derived from a fluorinated monomer which is other than the tetrafluoroethylene.
5. The method for producing a fluororesin film according to claim 4 , wherein the monomer having an adhesive functional group has a cyclic acid anhydride group.
6. The method for producing a fluororesin film according to claim 4 , wherein the fluorinated monomer is hexafluoropropylene or a monomer represented by CF 2 ═CFOR f1 , wherein R f1 is a C 1-10 perfluoroalkyl group, or a group having an etheric oxygen atom between carbon atoms of a C 2-10 perfluoroalkyl group.
7. The method for producing a fluororesin film according to claim 1 , wherein a melt flow rate of the fluororesin at the temperature of the extrusion die and at a load of 49N, is from 10 to 30 g/10 min.
8. The method for producing a fluororesin film according to claim 1 , wherein a melt flow rate stability S 60 of the fluororesin as obtained by formula (2) is from 0.7 to 1.0:
S 60 =MFR 60 /MFR 0 (2)
wherein MFR 60 is a melt flow rate of the fluororesin at the temperature of the extrusion die and at a load of 49N as measured with respect to the fluororesin after heating for 60 minutes at the temperature of the extrusion die in an air atmosphere, and
MFR 0 is a melt flow rate of the fluororesin at the temperature of the extrusion die and at a load of 49N as measured with respect to the fluororesin before heating for 60 minutes at the temperature of the extrusion die.
9. The method for producing a fluororesin film according to claim 1 , wherein a melt flow rate stability S 60 of the fluororesin as obtained by formula (2) is from 0.8 to 1.0:
S 60 =MFR 60 /MFR 0 (2)
wherein MFR 60 is a melt flow rate of the fluororesin at the temperature of the extrusion die and at a load of 49N as measured with respect to the fluororesin after heating for 60 minutes at the temperature of the extrusion die in an air atmosphere, and
MFR 0 is a melt flow rate of the fluororesin at the temperature of the extrusion die and at a load of 49N as measured with respect to the fluororesin before heating for 60 minutes at the temperature of the extrusion die.
10. The method for producing a fluororesin film according to claim 1 , wherein a melt flow rate of the fluororesin at 372° C. and at a load 49N as measured in accordance with JIS K7210; 1999, is from 20 to 50 g/10 min.
11. The method for producing a fluororesin film according to claim wherein a melt flow rate of the fluororesin at 372° C. and at a load 49N as measured in accordance with JIS K7210; 1999, is from 30 to 50 g/10 min.
12. The method for producing a fluororesin film according to claim 2 , wherein a melt flow rate stability S 60 of the fluororesin as obtained by formula (2) is from 0.7 to 1.3:
S 60 =MFR 60 /MFR 0 (2)
wherein MFR 60 is a melt flow rate of the fluororesin at the temperature of the extrusion die and at a load of 49N as measured with respect to the fluororesin after heating for 60 minutes at the temperature of the extrusion die in an air atmosphere, and
MFR 0 is a melt flow rate of the fluororesin at the temperature of the extrusion die and at a load of 49N as measured with respect to the fluororesin before heating for 60 minutes at the temperature of the extrusion die.
13. The method for producing a fluororesin film according to claim 2 , wherein a melt flow rate of the fluororesin at 372° C. and at a load 49N as measured in accordance with JIS K7210; 1999, is from 20 to 70 g/10 min.
14. The method for producing a fluororesin film according to claim 1 , wherein a melt flow rate stability S 60 of the fluororesin as obtained by formula (2) is from 0.7 to 1.3:
S 60 =MFR 60 /MFR 0 (2)
wherein MFR 60 is a melt flow rate of the fluororesin at the temperature of the extrusion die and at a load of 49N as measured with respect to the fluororesin after heating for 60 minutes at the temperature of the extrusion die in an air atmosphere, and
MFR 0 is a melt flow rate of the fluororesin at the temperature of the extrusion die and at a load of 49N as measured with respect to the fluororesin before heating for 60 minutes at the temperature of the extrusion die.
15. The method for producing a fluororesin film according to claim 12 , wherein a melt flow rate of the fluororesin at 372° C. and at a load 49N as measured in accordance with JIS K7210; 1999, is from 20 to 70 g/10 min.
16. The method for producing a fluororesin film according to claim 1 , wherein a melt flow rate of the fluororesin at 372° C. and at a load 49N as measured in accordance with JIS K7210; 1999, is from 20 to 70 g/10 min.
17. The method for producing a fluororesin film according to claim 14 , wherein a melt flow rate of the fluororesin at 372° C. and at a load 49N as measured in accordance with JIS K7210; 1999, is from 20 to 70 g/10 min.
18. The method for producing a fluororesin film according to claim 1 , wherein the fluororesin has an adhesive functional group.
19. The method for producing a fluororesin film according to claim 1 , wherein the extrusion die is a coat hanger die.
20. The method for producing a fluororesin film according to claim 1 , wherein the average flow velocity v 0.95 of the fluororesin material is from 6.58×10 −4 to 5×10 −2 m/sec.