Ion exchange polymer dispersion, process for its production and its use
View Patent ↗A thickened ion exchange polymer dispersion is obtained by applying ultrasonic vibration or a shearing force to an ion exchange polymer dispersion having a fluorinated polymer having sulfonic acid groups as an ion exchange polymer uniformly dispersed in a dispersion medium so that the viscosity of the dispersion at 25° C. at a shear rate of 10 (1/s) increases 2-2000 times in a thickening step. When formed into a membrane, the dispersion can forms an ion exchange membrane having a uniform and small thickness, high strength, which is free from cracking and shows constant swelling in water and steam. Further, a layer formed by applying a coating solution containing this dispersion and a catalyst powder comprising catalyst metal particles and a carbon support loaded with the catalyst metal particles to a substrate can be used to prepare a membrane-electrode assembly as a catalyst layer for at least one of the cathode and the anode by providing the catalyst layer adjacently to an ion exchange membrane. Because the catalyst layer is highly strong, has few defects and is excellently smooth, a high-performance membrane-electrode assembly for solid polymer electrolyte fuel cells can be obtained.
1. A process for preparing an ion exchange polymer dispersion comprising:
preparing a uniform dispersion of an ion exchange polymer having an initial viscosity;
filtering the uniform dispersion of an ion exchange polymer having an initial viscosity wherein coarse particles are removed from the uniform dispersion of an ion exchange polymer having an initial viscosity; and
applying either an ultrasonic vibration or a shearing force to the uniform dispersion of an ion exchange polymer to increase the viscosity to 2-2000 times the initial viscosity;
wherein
the filtering the uniform dispersion comprises filtering through a filter having a pore diameter of from 0.5 to 30 μm,
the uniform dispersion of an ion exchange polymer comprises a monohydric or a polyhydric alcohol,
the ion exchange polymer is a fluorinated polymer comprising sulfonic acid groups; and
the viscosity is measured at 25° C. at a shear rate of 10 (1/s), and wherein
if ultrasonic vibration is applied, a power of 30 to 2,000 W is applied to the uniform dispersion of an ion exchange polymer in the ultrasonic vibration, or
if the shearing force is applied to the uniform dispersion of an ion exchange polymer, the shearing force is in the range of 1,000 to 50,000 rpm.
2. The process for preparing an ion exchange polymer dispersion according to claim 1 , wherein the applying ultrasonic vibration comprises imparting energy in an amount from 0.01 to 10 kWh per 1 kg of unit mass of the uniform dispersion of an ion exchange polymer having an initial viscosity.
3. The process for preparing an ion exchange polymer dispersion according to claim 1 , wherein the applying shearing force comprises applying a shearing force at a shear rate of from 10 2 to 10 8 1/s.
4. The process for preparing an ion exchange polymer dispersion according to claim 3 , wherein the applying shearing force comprises imparting energy in an amount from 10 3 to 10 8 J per 1 kg of unit mass of the uniform dispersion of an ion exchange polymer having an initial viscosity.
5. The process for preparing an ion exchange polymer dispersion according to claim 1 further comprising adjusting the concentration of the uniform dispersion of an ion exchange polymer having an initial viscosity to from 3 to 40% in terms of mass ratio to the total mass before the applying the ultrasonic vibration or shearing force.
6. The process for preparing an ion exchange polymer dispersion according to claim 1 wherein the initial viscosity is from 50 to 10000 mPa·s and the viscosity 2-2000 times the initial viscosity is from 1000 to 100000 mPa·s at 25° C. and a shear rate of 10 1/s.
7. The process for preparing an ion exchange polymer dispersion according to claim 5 , wherein a solid content of the uniform dispersion of an ion exchange polymer at a viscosity 2-2000 times the initial viscosity is 3 to 40% in terms of the mass ratio to the total mass.
8. The process for preparing an ion exchange polymer dispersion according to claim 1 , wherein the fluorinated polymer is a copolymer comprising polymerization units derived from tetrafluoroethylene and polymerization units derived from CF 2 ═CF(OCF 2 CFX) m —O p —(CF 2 ) n SO 3 H, wherein X is a fluorine atom or a trifluoromethyl group, m is an integer of from 0 to 3, n is an integer of from 0 to 12, and p is 0 or 1, provided that when n is 0, p is also 0.
9. The process for preparing an ion exchange polymer dispersion according to claim 5 wherein the initial viscosity is from 50 to 10000 mPa·s and the viscosity 2-2000 times the initial viscosity is from 1000 to 100000 mPa·s at 25° C. and a shear rate of 10 1/s.