A method for preparing peroxide vulcanized fluororubber by nanoemulsion polymerization
A technology for vulcanizing fluororubber and nanoemulsion, which is applied in the field of nanoemulsion polymerization to prepare peroxide vulcanized fluororubber, can solve the problems of low solid content, affecting production efficiency, and reducing equipment utilization rate, so as to improve emulsion concentration and improve production efficiency. , the effect of improving cold resistance
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Embodiment 1
[0022] Example 1: 4 kg of non-ion water was added to a 10L container, 3.8 kg of structural formula was CF3O (CF (CF3) CF2O) 8CoonH4 fluororether carboxylate, 1.6 kg structural formula CF3O (CF (CF3) CF2O) 10 (CF3) CF2O) 10 CF2CF2O) 4CF3 fluororetal oil, stirred evenly at normal temperature, the aqueous solution of a microemulsion surfactant having a concentration of 57.4% is obtained.
Embodiment 2
[0023] Example 2: A 10L polymerization tank as an example, 6 kg of non-ionized water, 0.3 kg of Examples of 0.3 kg, and a vulcanization point monomer 4-bromo-3, 3, 4, 4, in the reaction kettle. - Tetrafluoro-1-butene 12g, 1,6-diiododexyl hexane 7g; nitrogen-replacement and vacuum treatment, after oxygen content of kettle is ≤ 20 ppm; to add mass ratio to the kettle 25:38 : 37 Tetrafluoroethylene, Fluoroethylene, hexafluoropropylene mixed monomer, until the kettle is 1.8 MPa; stirring, temperature rise to 80 ° C, the concentration of 5% ammonium sulfate initiator 140g begins to react, reaction Continuous addition of the monomer mixture to maintain the pressure at 1.8 MPa; when the reaction is stopped, the reaction is stopped, and the unreacted mixing monomer is recovered after cooling; the polymerized latex is condensed, washed, dried by the opening machine after drying. Oxide vulcanized fluoride rubber.
Embodiment 3
[0024] Example 3: Taking 20L polymerization tub as an example, 12 kg of no ionized water, 0.6 kg of Examples of 0.6 kg of Examples, 4-bromo-3, 3, 4, 4, in the reaction kettle. - Tetrafluoro-1-butene 24g, 1,6-diiododexyl hexane 14g; nitrogen-replacement and vacuum treatment, kettle internal oxygen content is ≤ 20 ppm; to the kettle to add mass ratio 25:38 : 37 Tetrafluoroethylene, Fluoroethylene, hexafluoropropene mixed monomer, until the kettle is 2.0 MPa; stirring, temperature rise to 82 ° C, add concentration of 5% ammonium sulfate initiator 300g to start reactions, reaction Continuous addition of the monomer mixture to maintain the pressure at 2.0 MPa; when the reaction is stopped, the reaction is stopped, and the unreacted mixing monomer is recovered; the polymerization of the obtained latex is condensed, washed, dried and dehydrated by the opening machine. Oxide vulcanized fluoride rubber.
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