Perfluoroether elastomer and preparation method thereof
A technology of elastomer and perfluoroether, which is applied in the field of preparation of fluoroelastomer to achieve the effect of increasing flexibility and enhancing crosslinking density
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Embodiment 1
[0031] In a 5L stainless steel reactor equipped with a stirrer, add 3L of deionized water, 2g of dipotassium hydrogen phosphate, 2g of emulsifier (a mixture of perfluoropolyether peroxide and sodium octyl sulfonate with a mass ratio of 1:1), After repeating nitrogen pressurization and evacuating and degassing, the mixed monomer of TFE / PMVE / PPVE=60 / 35 / 5 (molar ratio) was added to the reactor with a compressor, and the pressure was increased to 1.2 MPa at 80°C. 10g of perfluorobromoethyl vinyl ether and 10g of 15% (wt) ammonium persulfate aqueous solution were pumped into the pump to initiate the polymerization reaction. When the reactor pressure drops to 1.0MPa, add ICHF 2 CHF 2 I 5g, while adding VDF / HFP=80 / 20TFE / PMVE / PPVE=60 / 35 / 5 (molar ratio) of mixed monomers, keeping the pressure in the reactor at 1.2MPa.
[0032] As the reaction progresses, 10 g of the initiator aqueous solution, that is, 15% (wt) ammonium persulfate aqueous solution, is added once every 4 hours. The reacti...
Embodiment 2
[0039] In a 5L stainless steel reactor with a stirrer, add 3L of non-ionized water, 2g of dipotassium hydrogen phosphate, 2g of emulsifier (perfluoropolyether peroxide and sodium octyl sulfonate with a mass ratio of 1:1), repeat After pressurizing with nitrogen and evacuating and degassing, the mixed monomer of TFE / PMVE / PEVE=60 / 35 / 5 (molar ratio) is added to the reactor with a compressor, and the pressure is increased to 1.2 MPa at 80°C and passed through a metering pump 10g of perfluorobromoethyl vinyl ether and 10g of 15% (wt) ammonium persulfate aqueous solution were pressed into it to initiate the polymerization reaction. When the pressure of the reactor drops to 1.0MPa, add I(CF 2 CF 2 ) 2 I 8g, while adding TFE / PMVE / PEVE=60 / 35 / 5 (molar ratio) of mixed monomers, keeping the pressure in the reactor at 1.2 MPa.
[0040] As the reaction progresses, 10 g of 15% (wt) ammonium persulfate aqueous solution of initiator is added once every 4 h. The reaction lasted for about 10 hours...
Embodiment 3
[0044] In a 5L stainless steel reactor with a stirrer, add 3L of non-ionized water, 2g of dipotassium hydrogen phosphate, and 2g of emulsifier. After repeated nitrogen pressurization and evacuation and degassing, add TFE / PMVE / to the reactor with a compressor. PEVE / PPVE=65 / 30 / 2 / 3 (molar ratio) of mixed monomers, the pressure is increased to 1.2MPa at 80°C, and 10g of perfluorobromoethyl vinyl ether, 10g of 15% ( wt) Aqueous ammonium persulfate solution initiates the polymerization reaction, and when the pressure of the reactor drops to 1.0MPa, add I(CF 2 ) 5 I 4g was added at the same time with TFE / PMVE / PEVE / PPVE=65 / 30 / 2 / 3 (molar ratio) of mixed monomers, keeping the pressure in the reactor at 1.2MPa.
[0045] As the reaction progresses, 10 g of 15% (wt) ammonium persulfate aqueous solution of initiator is added once every 4 h. The reaction lasted for about 8 hours, and about 4.5 kg of elastomer emulsion was obtained. Agglomerate with sodium chloride aqueous solution, wash, and ...
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