Preparation method of wide-distribution polyvinylidene fluoride
A polyvinylidene fluoride and vinylidene fluoride technology, applied in the field of preparation of fluorine-containing polymers, can solve the problems of low possibility of industrialization, narrow molecular weight distribution, poor processing performance, etc., and achieve high physical and mechanical properties, wide molecular weight distribution, The effect of good processability
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Embodiment 1
[0027] In a 5L horizontal stainless steel jacketed and stirred polymerization reactor, add about 0.10wt% ammonium perfluorooctanoate and 0.03wt% paraffin wax accounting for the total mass of the monomers, and replace the nitrogen gas by vacuuming 5 times. The oxygen content in the kettle is lower than 20ppm, and the vinylidene fluoride monomer is added to maintain the system at an atmospheric pressure, the stirring is started, and the temperature is raised to a polymerization temperature of 75°C. 18.75wt% VDF monomer accounting for the total mass of the monomer was introduced to make the pressure of the reactor 4.50MPa. Add the IPP initiator solution with a volume fraction of 6.50% to the reactor through a parallel flow pump. Within 10 minutes of the polymerization reaction, the pressure drop was 0.07MPa, and the VDF monomer was continuously added to maintain the system pressure at 4.50MPa, and a certain amount of IPP initiator solution was supplemented to maintain a certain p...
Embodiment 2
[0033]In a 5L horizontal stainless steel jacketed and stirred polymerization reactor, add about 0.10wt% ammonium perfluorooctanoate and 0.03wt% paraffin wax accounting for the total mass of the monomers, and replace the nitrogen gas by vacuuming 5 times. The oxygen content in the kettle is lower than 20ppm, and the vinylidene fluoride monomer is added to maintain the system at an atmospheric pressure, the stirring is started, and the temperature is raised to a polymerization temperature of 80°C. 18.75wt% VDF monomer accounting for the total mass of the monomer was introduced to make the pressure of the reactor 4.50MPa. Add the IPP initiator solution with a volume fraction of 6.50% to the reactor through a parallel flow pump. Within 10 minutes of the polymerization reaction, the pressure drop was 0.07MPa, and the VDF monomer was continuously added to maintain the system pressure at 4.50MPa, and a certain amount of IPP initiator solution was supplemented to maintain a certain po...
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