Polyvinylidene fluoride resin with fluorine ether end group structure and preparation method thereof
A technology of polyvinylidene fluoride and vinylidene fluoride, which is applied in the field of manufacturing polyvinylidene fluoride resin, and can solve problems such as wide product molecular weight distribution, general end group stability, and insufficient stability
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Embodiment 1
[0079] Firstly, vinylidene fluoride and perfluoro-n-propyl vinyl ether are formulated into a mixed monomer according to the ratio of perfluoro-n-propyl vinyl ether content to 5 mol%, and placed in a monomer tank for later use, and the temperature of the mixed monomer is controlled at 45°C.
[0080] In the 1.2L reactor, first pass cold brine at -15°C in the jacket to control the temperature of the reactor at -5°C, then add 720g of 2,3-dihydrodecafluoropentane (HFC4310mee), and close the kettle Then start stirring, the stirring speed is 700rpm, replace the air with nitrogen, after the oxygen content is less than 50ppm, put hot water in the jacket, and control the reaction temperature at 35°C, then add the prepared mixed monomer to a pressure of 0.5 MPa, add 73.1g comonomer (60g vinylidene fluoride and 13.1g perfluoro n-propyl vinyl ether monomer) altogether, add 1.5g (CF 3 CF(OCF 2 CF 2 CF 3 )COO) 2 Initiator, after the pressure drop occurs, start to add monomer to maintain ...
Embodiment 2
[0083] Firstly, vinylidene fluoride and perfluoro-n-propyl vinyl ether are formulated into a mixed monomer according to the ratio of perfluoro-n-propyl vinyl ether content to 8 mol%, and placed in a monomer tank for later use. The temperature of the mixed monomer is controlled at 45°C.
[0084] In the 25L reactor, first pass cold brine at -15°C in the jacket to control the temperature of the reactor at -5°C, and then add 12.5kg of 1,1,1,3,3-pentafluorobutane (HFC365mfc ), start stirring after closing the kettle, the stirring speed is 800rpm, and replace the air with nitrogen. body to a pressure of 0.75MPa, a total of 1.702kg comonomers (1.25kg vinylidene fluoride and 0.452kg perfluoro-n-propyl vinyl ether monomer) were added, and 22.7g (CF 3 CF(OCF 2 CF 2 CF 3 )COO) 2 Initiator, after the pressure drop occurs, start to add monomers to maintain the reaction pressure at 0.75MPa. After the amount of added monomers reaches 375g, stop feeding, lower the system temperature to 10°C...
Embodiment 3
[0087] With embodiment 1, just add trifluorotrichloroethane (CFC113) as solvent, with [CF 3 CF(OCF 3 )COO] 2 As an initiator, perfluoromethyl vinyl ether is used as a comonomer.
[0088] First, vinylidene fluoride and perfluoromethyl vinyl ether are formulated into a mixed monomer according to the ratio of perfluoromethyl vinyl ether content of 12.4 mol%, and placed in a monomer tank for standby, and the temperature of the mixed monomer is controlled at 45°C.
[0089] In the 1.2L reactor, first pass cold brine at -15°C in the jacket to control the temperature of the reactor at -5°C, then add 636g of trifluorotrichloroethane, start stirring after closing the kettle, and the stirring speed is 650rpm, replace the air with nitrogen, after the oxygen content is less than 50ppm, pass hot water into the jacket, and control the reaction temperature at 30°C, then add the prepared mixed monomer to a pressure of 0.5MPa, and add a total of 154.5g copolymerization monomer (including 113...
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