High melt strength acrylic resin and preparation
A technology of polypropylene resin and high melt strength, which is applied in the field of high melt strength polypropylene resin and its preparation, which can solve the problems of high gel content, decreased mechanical properties, difficult control of polypropylene degradation, etc., and achieve good effect , improved melt strength, and easy implementation
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Embodiment 1
[0045] Embodiment 1 (adding iron dimethyl dithiocarbamate)
[0046] Get 45g original ecological powder (homopolypropylene powder, melt index is 7.1g / 10min), 0.05g trimethylolpropane triacrylate, 0.02g iron dimethyl dithiocarbamate, in high-speed mixer Mix evenly in medium for 20 minutes, add it into the material chamber of the internal mixer, set the temperature at 200°C, rotate at 80 rpm, and discharge with stable torque after 7 minutes of reaction time. The results are shown in Table 1.
Embodiment 2
[0049] Embodiment 2 (add iron dimethyl dithiocarbamate)
[0050] 100 parts by weight of polypropylene (homopolypropylene powder, melt index is 7.1g / 10min), 0.20 parts by weight of iron dimethyl dithiocarbamate, 1.50 parts by weight of trimethylolpropane triacrylic acid The ester is mixed evenly in a high-speed mixer for 20 minutes. Add it to a twin-screw extruder with L / D=40 and Φ of 24 mm. The rotation number of the extruder is set at 240 rpm. The extruder is divided into eight The heating zones are respectively: 175°C, 190°C, 200°C, 220°C, 230°C, 230°C, 230°C, 220°C, extruded and granulated to obtain high melt strength polypropylene resin. The results are shown in Table 1.
Embodiment 3
[0052] Get 45g original ecological powder, (homopolypropylene powder, melt index is 7.1g / 10min) 4.50g ethoxylated trimethylolpropane triacrylate, 0.06g copper dimethyl dithiocarbamate, Mix evenly in a high-speed mixer for 20 minutes, add to the material chamber of the internal mixer, set the temperature at 210°C, rotate at 20 rpm, and discharge with stable torque after 7 minutes of reaction time. The results are shown in Table 1.
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