Production method of tetrafluoroethylene polymer used for processing wide breadth oilless low-density raw material sealing belt
A technology with tetrafluoroethylene and tetrafluoroethylene, applied in the field of polymers, can solve the problems of uneven thickness, uneven rolling width, poor appearance, etc., and achieve the effect of good emulsion stability and stable resin performance
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Embodiment 1
[0025] In a 800L polymerization kettle with a stirrer, add 520L of deionized water, 36Kg of paraffin, 2500ml of 30% (percentage by weight) ammonium perfluorooctanoate solution, 4g of ammonium persulfate, 312g of succinic anhydride, airtightly evacuate and replace with nitrogen, after analyzing oxygen After the content is less than or equal to 30ppm, the temperature in the reactor is raised to 70°C, and TFE monomer (30ppm of difluoromethane and 5ppm of trifluoroethylene) is added until the pressure in the kettle is 2.0Mpa. Under constant stirring conditions, constant pressure The reaction is carried out under the following conditions. During the reaction process, since TFE polymerization is a strong exothermic reaction, the heat needs to be taken away by circulating water to control the temperature in the kettle to rise steadily. As the reaction progresses, the temperature in the kettle continues to rise. When the reaction kettle When the temperature reaches 100°C, the reaction ...
Embodiment 2
[0027] In a 2000L polymerization kettle with agitator, add 1300L of deionized water, 60Kg of paraffin, 5000ml of 30% (percentage by weight) ammonium perfluorooctanoate solution, 10g of ammonium persulfate, 1300g of succinic anhydride, airtightly evacuate and replace with nitrogen, and analyze the oxygen content After the 30ppm or less is qualified, raise the temperature in the reactor to 65°C, add TFE monomer (50ppm of difluoromethane and 10ppm of trifluoroethylene) until the pressure in the kettle is 2.0Mpa, under constant stirring conditions and constant pressure The reaction is carried out. During the reaction process, since TFE polymerization is a strong exothermic reaction, it is necessary to use circulating water to take away the heat and control the temperature in the kettle to rise steadily. As the reaction progresses, the temperature in the kettle continues to rise. When the temperature in the reactor Stop the reaction when it reaches 95°C, the reaction TFE amount is 5...
Embodiment 3
[0029] In a 2000L polymerization kettle with agitator, add 1300L of deionized water, 60Kg of paraffin, 5000ml of 30% (percentage by weight) ammonium perfluorooctanoate solution, 10g of ammonium persulfate, 1300g of succinic anhydride, airtightly evacuate and replace with nitrogen, and analyze the oxygen content After 30ppm or less is qualified, raise the temperature in the reactor to 65°C, add TFE monomer (difluoromethane in mass: 80ppm, trifluoroethylene: 17ppm) until the pressure in the kettle is 2.5Mpa, under constant stirring conditions, constant The reaction is carried out under pressure. During the reaction process, since TFE polymerization is a strong exothermic reaction, the heat needs to be taken away by circulating water to control the temperature in the kettle to rise steadily. As the reaction progresses, the temperature in the kettle continues to rise. When the reaction kettle Stop the reaction when the internal temperature reaches 95°C, the amount of TFE reacted is...
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