A modified fluoroelastomer, its preparation method and application
An elastomer and modification technology, applied in the field of modified fluoroelastomers, can solve the problem that fluororubber is difficult to fundamentally improve its performance.
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Embodiment 1
[0045] Add 3L of deionized water, 1.5g of perfluorooctanoic acid, 1.5g of disodium hydrogen phosphate and 540g of heptaaminovinyl POSS into a 5L reactor. The temperature of the reactor was raised to 60° C., and the reaction monomer was charged to 2.5 MPa with a gas composition of 48 wt % vinylidene fluoride (VDF), 47 wt % hexafluoropropylene (HFP), and 5 wt % chlorotrifluoroethylene. Subsequently, 40 mL of 10 wt % ammonium persulfate initiator aqueous solution was continuously added at a rate of 10 mL / h. During the reaction process, the gas reaction monomer was continuously added to maintain the pressure of the reactor at 2.5 MPa. When the addition of the gas reaction monomer reached 30% of the total weight of the reaction, 9g of chloroform was added. During the reaction process, a total of 1300 g of gaseous reactive monomers were added to the reactor, and the total reaction time was 4 hours. The polymerized emulsion was demulsified, washed and dried to obtain 1150 g of POSS...
Embodiment 2
[0048] 3L of deionized water, 75g of ammonium perfluorooctanoate, 30g of potassium dihydrogen phosphate and 180g of hepta(tetramethylammoniumoxy)propenyl POSS were added to a 5L reactor. The temperature of the reactor was raised to 100° C., and the gaseous reaction monomer was composed of 65wt% vinylidene fluoride (VDF), 32wt% hexafluoropropylene (HFP) and 3wt% trifluoroethylene, and the pressure was charged to 3.5MPa. Subsequently, 40 mL of 10 wt % potassium persulfate initiator aqueous solution was continuously added at a rate of 10 mL / h. During the reaction process, the gas reaction monomer was continuously added to maintain the pressure of the reactor at 3.5 MPa. When the addition of the gas reaction monomer reached 35% of the total weight of the reaction, 9g of diethyl malonate was added. During the reaction process, a total of 1500 g of gas reaction monomers were added to the reactor, and the total reaction time was 4 hours. The polymerized emulsion was demulsified, wa...
Embodiment 3
[0051] Add 3L of deionized water, 15g of potassium perfluorooctanoate, 45g of sodium tetraborate and 15g of heptaanilinemethylbutenyl POSS into a 5L reactor. Reactor was heated up to 90°C, with 40wt% vinylidene fluoride (VDF), 53wt% hexafluoropropylene (HFP), 7wt% BrCF 2 CF 2 CH=CH 2 The gas reaction monomer is charged to 1.3MPa. Subsequently, 40 mL of 10 wt % ammonium persulfate initiator aqueous solution was continuously added at a rate of 10 mL / h. During the reaction process, the gas reaction monomer was continuously added to maintain the pressure of the reactor at 1.3MPa. When the addition amount of the gas reaction monomer reached 10% of the total weight of the reaction, 9 g of isopentane was added. During the reaction process, a total of 1300 g of gaseous reactive monomers were added to the reactor, and the total reaction time was 4 hours. The polymerized emulsion was demulsified, washed and dried to obtain 1150 g of POSS modified fluoroelastomer.
[0052] After te...
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