Preparation method of high fluidity modified polychlorotrifluoroethylene resin
A technology of polychlorotrifluoroethylene and chlorotrifluoroethylene, which is applied in the field of preparation of high-fluidity modified polychlorotrifluoroethylene resin, can solve the problem that the transparency and melt fluidity are not improved, and the uniformity of the polymer state cannot be guaranteed , product performance instability and other issues, to achieve the effect of improving melt fluidity and transparency, improving processing fluidity, and easy molding control
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Embodiment 1
[0029] Taking a 10L high-pressure reactor as an example, add 5L of deionized water, 25g of potassium dihydrogen phosphate, vacuumize, replace oxygen with nitrogen, start stirring at a stirring speed of 400rpm, add 2kg of chlorotrifluoroethylene monomer and 22g of perfluoropropylethylene base ether, then dissolve 22g of azobisisobutylamidine hydrochloride with deionized water and mix evenly, then add it to the reaction kettle, raise the temperature to 55°C, control the reaction temperature at 55°C±1°C, and stop the reaction after stirring for 10 hours , release the pressure to obtain powdery polychlorotrifluoroethylene resin, wash and dry the obtained resin.
[0030] Add 0.1 wt% of fluorochloro oil with a molecular weight of 9000 and 0.1 wt% of boron nitride with a particle size of 0.3 μm to the resin obtained above, mix uniformly in a high-speed mixer, granulate through a screw extruder, and extrude The extruder barrel temperature is 260°C-310°C, the screw speed is 100rpm, the...
Embodiment 2
[0032] Take a 10L high-pressure reactor as an example, add 5L deionized water, 25g potassium dihydrogen phosphate, vacuumize, replace oxygen with nitrogen, start stirring at a stirring speed of 500rpm, add 2kg of chlorotrifluoroethylene monomer and 28g of perfluoromethylethylene base ether, then dissolve 28g of azobisisobutylamidine hydrochloride with deionized water and mix evenly, then add it to the reaction kettle, raise the temperature to 40°C, control the reaction temperature at 40°C±1°C, and stop the reaction after stirring for 11 hours , release the pressure to obtain powdery polychlorotrifluoroethylene resin, wash and dry the obtained resin.
[0033] Add 0.1wt% of perfluoropolyether with a molecular weight of 9800 and 0.35wt% of talcum powder with a particle size of 0.5 μm to the above-mentioned obtained resin, mix uniformly in a high-speed mixer, granulate through a screw extruder, and extrude The extruder barrel temperature is 260°C-310°C, and the screw speed is 100r...
Embodiment 3
[0035] Take a 10L high-pressure reactor as an example, add 5L deionized water, 20g sodium dihydrogen phosphate, vacuumize, replace oxygen with nitrogen, start stirring at a stirring speed of 500rpm, add 2kg of chlorotrifluoroethylene monomer and 15g of perfluoroethylethylene base ether, then dissolve 16g of azobisisobutylamidine hydrochloride with deionized water and mix evenly, then add it to the reaction kettle, raise the temperature to 62°C, control the reaction temperature at 62°C±1°C, and stop the reaction after stirring for 9 hours , release the pressure to obtain powdery polychlorotrifluoroethylene resin, wash and dry the obtained resin.
[0036]Add 0.5wt% of fluorochloro oil with a molecular weight of 8200 and 0.5wt% of boron nitride with a particle size of 0.3 μm to the resin obtained above, mix uniformly in a high-speed mixer, granulate through a screw extruder, and extrude The extruder barrel temperature is 260°C-310°C, the screw speed is 100rpm, the material is mel...
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