A kind of modified PTFE dispersion resin and preparation method thereof
A dispersing resin and modification technology, which is applied in the field of modified PTFE dispersing resin and its preparation, can solve the problems of shortened service life, uneven mechanical properties, affecting product weight, etc., and achieve lower extrusion pressure and good paste extrusion performance, and the effect of improving thermal stability
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Embodiment 1
[0039] 1m 3 700L of deionized water, 30kg of paraffin, 200g of perfluorooctanoic acid ammonium, and 500g of surface fluorinated silica nanoparticles were added to the stainless steel reaction kettle. Carry out nitrogen replacement and vacuum treatment to the polymerization kettle, and analyze the oxygen content. When the oxygen content is less than or equal to 10ppm, it is qualified. Then 700g of PPVE was added, the temperature of the reactor was raised to 70°C, stirring was started, TFE monomer was added to 1.8MPa, and the stirring rate was 280rpm. After reaching the specified temperature and pressure, add 3g of initiator ammonium persulfate (dissolved in 20g of deionized water) and 60g of succinic acid peroxide dissolved in deionized water, and the reaction starts. During the whole reaction process, the pressure of the polymerization tank was kept at 1.8MPa±0.05MPa. When the reaction was carried out until the consumption of TFE was 20 kg, the monomer in the gas phase was r...
Embodiment 2
[0041] 1m 3 700L of deionized water, 30kg of paraffin, 200g of perfluorooctanoic acid ammonium, and 500g of surface fluorinated silica nanoparticles were added to the stainless steel reaction kettle. Carry out nitrogen replacement and vacuum treatment to the polymerization kettle, and analyze the oxygen content. When the oxygen content is less than or equal to 10ppm, it is qualified. Then 1600g of PPVE was added, the temperature of the reactor was raised to 70°C, stirring was started, TFE monomer was added to 1.8MPa, and the stirring rate was 280rpm. After reaching the specified temperature and pressure, add 3g of initiator ammonium persulfate (dissolved in 20g of deionized water) and 60g of succinic acid peroxide dissolved in deionized water, and the reaction begins. During the whole reaction process, the pressure of the polymerization tank was kept at 1.8MPa±0.05MPa. When the reaction was carried out until the consumption of TFE was 20 kg, the monomer in the gas phase was ...
Embodiment 3
[0043] 1m 3 700L of deionized water, 30kg of paraffin, 200g of perfluorooctanoic acid ammonium, and 500g of surface fluorinated silica nanoparticles were added to the stainless steel reaction kettle. Carry out nitrogen replacement and vacuum treatment to the polymerization kettle, and analyze the oxygen content. When the oxygen content is less than or equal to 10ppm, it is qualified. Then 100g of PPVE was added, the temperature of the reactor was raised to 70°C, stirring was started, TFE monomer was added to 1.8MPa, and the stirring rate was 280rpm. After reaching the specified temperature and pressure, add 3g of initiator ammonium persulfate (dissolved in 20g of deionized water) and 60g of succinic acid peroxide dissolved in deionized water, and the reaction begins. During the whole reaction process, the pressure of the polymerization tank was kept at 1.8MPa±0.05MPa. When the reaction was carried out until the consumption of TFE was 20 kg, the monomer in the gas phase was r...
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