Ternary peroxide fluororubber and preparation method thereof, and intelligent wearable material and preparation method thereof
A ternary peroxyfluororubber and peroxyfluororubber technology, which is applied in applications, clothing, jewelry, etc., can solve the problems that wristbands and watchbands cannot meet the requirements of safety, environmental protection, durability, and physical comfort.
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Embodiment 1
[0081] Carry out in the high pressure polymerization reactor of 10L, the total weight of vinylidene fluoride, tetrafluoroethylene and hexafluoropropylene added in the present embodiment is 2.3Kg, and the concrete steps are:
[0082] A1. Add 5L of deionized water, 4g of dipotassium hydrogen phosphate, 4g of diiodomethane and 10g of perfluoropolyether carboxylate ammonium salt (10wt%) into the high-pressure polymerization reaction kettle, evacuating nitrogen for replacement, and the oxygen in the high-pressure polymerization reaction kettle The content is reduced to less than 25ppm, and the temperature of the reactor is raised to 85°C;
[0083] A2, add initial monomers (vinylidene fluoride, tetrafluoroethylene and hexafluoropropylene) into the high-pressure polymerization reaction kettle with a compressor until the pressure in the high-pressure polymerization reaction kettle is 2.0Mpa, start stirring, and adjust the rotational speed to be 98rpm;
[0084] A3. When the mixture in ...
Embodiment 2
[0088] The present embodiment is carried out in a 10L high-pressure polymerization reactor, and the total weight of vinylidene fluoride, tetrafluoroethylene and hexafluoropropylene added in the present embodiment is 2.3Kg, and the specific steps are:
[0089] A1, add 5L deionized water, 5g dipotassium hydrogen phosphate, 6g diiodomethane and 9g perfluoropolyether carboxylate ammonium salt (10wt%) in the high pressure polymerization reaction kettle, evacuate nitrogen replacement, and replace the oxygen in the high pressure polymerization reaction kettle with oxygen The content is reduced to less than 25ppm, and the temperature of the reactor is raised to 83°C;
[0090] A2, adding initial monomers (vinylidene fluoride, tetrafluoroethylene and hexafluoropropylene) to the high-pressure polymerization reactor with a compressor to the pressure in the high-pressure polymerization reactor is 2.2Mpa, start stirring, and adjust the rotating speed to be 100rpm;
[0091] A3. When the mixt...
Embodiment 3
[0095] The present embodiment is carried out in a 10L high-pressure polymerization reactor, and the total weight of vinylidene fluoride, tetrafluoroethylene and hexafluoropropylene added in the present embodiment is 2.3Kg, and the specific steps are:
[0096] A1. Add 5L of deionized water, 5g of dipotassium hydrogen phosphate, 6g of diiodomethane and 11g of perfluoropolyether carboxylate ammonium salt (10wt%) into the high-pressure polymerization reaction kettle, and evacuated nitrogen replacement to reduce the oxygen content in the reaction kettle to less than 25ppm, and the temperature of the reactor was raised to 70°C;
[0097] A2, adding initial monomers (vinylidene fluoride, tetrafluoroethylene and hexafluoropropylene) to the high-pressure polymerization reactor with a compressor to the pressure in the high-pressure polymerization reactor is 2.7Mpa, start stirring, and adjust the rotating speed to be 105rpm;
[0098] A3. When the mixture in the high-pressure polymerizatio...
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