Heat-proof ABS resin composition for blow-molding and preparation method thereof
An ABS resin, blow molding technology, applied in the field of heat-resistant ABS resin composition and its preparation, can solve the problems of high melt strength, impact resistance and tensile properties, and achieve the effect of high melt strength
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Embodiment 1
[0027] 35KgABS rubber powder, 45KgAS resin, terpolymer of 15KgN-phenylmaleimide, maleic anhydride and styrene, 5Kg acrylic copolymer, 0.1Kg bisphenol A, 0.1Kg IG-168 were added to After stirring in a high-speed mixer for 20 minutes, the material is discharged, and then extruded and granulated in a twin-screw extruder with an aspect ratio of 36 and a diameter of 35 mm. The barrel temperature of the extruder is 180-280 ° C, and the screw speed is 180-600rpm.
Embodiment 2
[0029] In order to better reflect the characteristics of the above-mentioned heat-resistant ABS resin composition for blow molding, and to compare the influence of different heat-resistant agent dosages on product performance, Example 2 is used here. In this embodiment, the terpolymer of N-phenylmaleimide identical with embodiment 1 and maleic anhydride and styrene is selected as the heat resistant agent, and the addition is changed from 15 parts in embodiment 1 to It is 5 parts, and the specific production is as follows: 35KgABS rubber powder, 55KgAS resin, 5KgN-phenylmaleimide, maleic anhydride and styrene terpolymer, 5Kg acrylic copolymer, 0.1Kg bisphenol A, 0.1Kg IG-168, join in the high-speed mixer and stir for 20 minutes and discharge, then extrude and granulate in a twin-screw extruder with a length-to-diameter ratio of 36 and a diameter of 35mm. The barrel temperature of the extruder is 180-280°C, the screw speed is 180-600rpm.
Embodiment 3
[0031] In order to better reflect the characteristics of the above-mentioned heat-resistant ABS resin composition for blow molding, and to compare the effects of different amounts of heat-resistant agents, Example 3 is used here. In this embodiment, the terpolymer of N-phenylmaleimide identical with embodiment 1 and maleic anhydride and styrene is selected as the heat resistant agent, and the addition is changed from 15 parts in embodiment 1 to 25, the specific production is as follows: 35KgABS rubber powder, 35KgAS resin, 25KgN-phenylmaleimide, maleic anhydride and styrene terpolymer, 5Kg acrylic copolymer, 0.1Kg bisphenol A, 0.1 Kg IG-168, added to the high-speed mixer and stirred for 20 minutes, then discharged, then extruded and pelletized in a twin-screw extruder with a length-to-diameter ratio of 36 and a diameter of 35mm. The barrel temperature of the extruder was 180 -280°C, the screw speed is 180-600rpm.
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