Preparation method of high-strength polychlorotrifluoroethylene
A polychlorotrifluoroethylene and chlorotrifluoroethylene technology, which is applied in the field of preparation of high-strength polychlorotrifluoroethylene, can solve the problem that it is difficult to prepare high-molecular-weight polychlorotrifluoroethylene, and it is difficult to prepare high-mechanical strength polychlorotrifluoroethylene. chlorotrifluoroethylene and other problems to achieve the effect of improving stability
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Embodiment 1
[0013] In a 5-liter vertical SUS316L stainless steel polymerization reactor, add 2 kg of deionized water, 2 kg of 1,1-dihydro-perfluoro-1-heptanol, and 0.6 g of 2,2-dihydro-perfluoro-ammonium heptanoate , 1.2 grams of bis(1,1-dichloro-perfluorobutyl) peroxide, the stirring speed is controlled to be 250 rpm, after deoxidation treatment, the inner temperature of the polymerization kettle is controlled at -10°C, and trifluorochlorine is continuously introduced Ethylene gas, so that the pressure in the kettle is 0.2MPa. When accumulatively 1.2 kilograms of chlorotrifluoroethylene monomers were added into the polymerization kettle, the feeding of chlorotrifluoroethylene was stopped, and the reaction was finished after 1 hour. The total polymerization time was 12 hours. The residual chlorotrifluoroethylene gas in the kettle is recovered, the pressure of the kettle is reduced to normal pressure, and the polymerized polychlorotrifluoroethylene is released to be fully washed and dried...
Embodiment 2
[0016] In a 5-liter vertical SUS316L stainless steel polymerization reactor, add 3 kg of deionized water, 2 kg of 1,1-dihydro-perfluoro-1-heptanol, and 0.15 g of 2,2-dihydro-perfluoro-ammonium heptanoate , 0.75 g of bis(1,1-dichloro-perfluorobutyl) peroxide, the stirring speed is controlled to be 250 rpm, after deoxidation treatment, the inner temperature of the polymerization kettle is controlled at -5°C, and trifluorochloro Ethylene gas, so that the pressure in the kettle is 0.24MPa. When accumulatively 1.57 kilograms of chlorotrifluoroethylene monomers were added into the polymerization kettle, the feeding of chlorotrifluoroethylene was stopped, and the reaction was finished after 1 hour. The total polymerization time was 12 hours. The residual chlorotrifluoroethylene gas in the kettle is recovered, the pressure of the kettle is reduced to normal pressure, and the polymerized polychlorotrifluoroethylene is released to be fully washed and dried to obtain a finished product....
Embodiment 3
[0019] In a 5-liter vertical SUS316L stainless steel polymerization reactor, add 2.5 kg of deionized water, 2 kg of 1,1-dihydro-perfluoro-1-heptanol, and 1.57 g of 2,2-dihydro-perfluoro-ammonium heptanoate , 1.18 grams of bis(1,1-dichloro-perfluorobutyl) peroxide, the stirring speed is controlled to be 250 rpm, after deoxidation treatment, the internal temperature of the polymerization kettle is controlled at -7°C, and trifluorochlorine is continuously introduced Ethylene gas, so that the pressure in the kettle is 0.224MPa. When accumulatively 1.57 kilograms of chlorotrifluoroethylene monomers were added into the polymerization kettle, the feeding of chlorotrifluoroethylene was stopped, and the reaction was finished after 1 hour. The total polymerization time was 12 hours. The residual chlorotrifluoroethylene gas in the kettle is recovered, the pressure of the kettle is reduced to normal pressure, and the polymerized polychlorotrifluoroethylene is released to be fully washed ...
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