A kind of tetrafluoroethylene and ethylene copolymer emulsion and preparation method thereof
A technology of ethylene copolymer and tetrafluoroethylene, which is applied in the field of preparation of self-emulsifying tetrafluoroethylene and ethylene copolymer emulsion, can solve problems such as the destruction of atmospheric ozone layer, unfavorable environmental protection and human health, and restricting the development of ETFE synthesis by solution method. , to achieve the effect of reducing crystallinity, improving tear resistance and good stability
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Embodiment 1
[0014] Add 10 liters of ion-free water to a 20-liter high-pressure polymerization kettle, add 1 mol of undecylenic acid and 1 mol of sodium hydroxide, vacuumize and replace the oxygen in the autoclave with nitrogen, heat up the temperature of the polymerization kettle to 50°C, and control the feeding valve to add The initial monomer of tetrafluoroethylene ethylene with a molar ratio of 45 / 55, until the internal pressure of the reactor is 3Mpa. Use a metering pump to add 30 ml of 5% initial initiator potassium persulfate aqueous solution, start polymerization, open the additional monomer (tetrafluoroethylene and ethylene molar ratio is 39 / 61) feed valve to continuously add monomer, open the additional The initiator metering pump continuously replenishes the initiator, adjusts the flow rate of the metering pump, finishes 350 ml of 5% potassium persulfate solution within 4 hours of polymerization time, controls the cooling water flow rate, and maintains the polymerization temperat...
Embodiment 2
[0017] Add 10 liters of ion-free water to a 20-liter high-pressure polymerization kettle, add 240 grams of undecylenic acid and 55 grams of sodium hydroxide, vacuumize and replace the oxygen in the autoclave with nitrogen, and the temperature of the polymerization kettle is raised to 60 ° C. Control the feeding The valve feeds the initial tetrafluoroethylene ethylene monomer with a molar ratio of 50 / 50 until the internal pressure of the reactor is 3.2Mpa. Use a metering pump to add 30 ml of 5% initial initiator potassium persulfate aqueous solution to start polymerization, open the additional monomer (tetrafluoroethylene and ethylene molar ratio is 40 / 60) feed valve to continuously add monomer, open the additional The initiator metering pump continuously replenishes the initiator, adjusts the flow rate of the metering pump, finishes 350 ml of 5% potassium persulfate solution within 4 hours of polymerization time, controls the flow rate of cooling water, and maintains the polyme...
Embodiment 3
[0020] Add 10 liters of ion-free water to a 20-liter high-pressure polymerization kettle, add 60 grams of crotonic acid and 50 grams of sodium hydroxide, vacuumize and replace the oxygen in the autoclave with nitrogen, heat the polymerization kettle to 70 ° C, and control the feeding valve to add The initial monomer of tetrafluoroethylene ethylene with a molar ratio of 48 / 52, until the internal pressure of the reactor is 3.5Mpa. Use a metering pump to add 35 ml of 5% initial initiator potassium persulfate aqueous solution, start polymerization, open the additional monomer (tetrafluoroethylene and ethylene molar ratio is 41 / 59) feed valve to continuously add monomer, open the additional The initiator metering pump continuously replenishes the initiator, adjusts the flow rate of the metering pump, finishes 350 ml of 5% potassium persulfate solution within 4 hours of polymerization time, controls the flow rate of cooling water, and maintains the polymerization temperature at 70°C ...
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