Smokeless non-halogen retardant polyolefine preparing method
A polyolefin and polyolefin resin technology, applied in the field of polymer composite materials in chemical materials, can solve the problems of low tensile strength, reduced tensile strength, damage to the mechanical properties of materials, etc., and achieve high elongation at break and low smoke characteristics. The effect of excellent, good mechanical properties
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Embodiment 1
[0023] The polymer grafts with reactive functional groups are prepared first. The density of weighing 99 parts is 0.918g / cm 3 , linear low density polyethylene with a melt index of 2.0g / 10min (190°C, 2.16kg), 0.5 parts of vinyl-tris(2-methoxyethoxy) silane, 0.5 parts of dicumyl peroxide and peroxide A mixture of benzoyl peroxide, wherein the weight ratio of dicumyl peroxide to benzoyl peroxide is 4:1. The raw materials according to the above proportions are uniformly mixed in a high-speed mixer for 10 minutes without heating during the mixing process, and then extruded, drawn, cooled and granulated on an ordinary twin-screw extruder. The temperature range of the extruder is set; the barrel is between 110°C and 200°C, and the head and die are between 210°C and 220°C.
[0024] Take by weighing 30 parts of reactive polymer grafts, 70 parts of ethylene vinyl acetate with VA content of 28%, 140 parts of unmodified aluminum hydroxide (average particle diameter 1.3 μm), silicon dio...
Embodiment 2
[0026] The polymer grafts with reactive functional groups are prepared first. Weigh 92.5 parts of ethylene vinyl acetate copolymer with a melt index of 0.65g / 10min (190°C, 2.16kg), 5 parts of vinyl-tris(2-methoxyethoxy)silane, 2.5 parts of peroxide A mixture of dicumyl peroxide and benzoyl peroxide, wherein the weight ratio of dicumyl peroxide to benzoyl peroxide is 4:1. The raw materials according to the above proportions are uniformly mixed in a high-speed mixer for 10 minutes without heating during the mixing process, and then extruded, drawn, cooled and granulated on an ordinary twin-screw extruder. The temperature range setting of the extruder: the barrel is between 110°C and 200°C, and the head and die are between 210°C and 220°C.
[0027] Take by weighing 50 parts of reactive polymer grafts, 50 parts of ethylene vinyl acetate with VA content of 28%, 160 parts of unmodified aluminum hydroxide (average particle diameter 1.3 μm), silicon dioxide (average particle diameter...
Embodiment 3
[0029]The polymer grafts with reactive functional groups are prepared first. Weigh 85 parts of polypropylene with a melt index of 3.0g / 10min (190°C, 2.16kg), 10 parts of vinyl-tris(2-methoxyethoxy)silane, 5 parts of dicumyl peroxide and A mixture of benzoyl peroxide, wherein the weight ratio of dicumyl peroxide to benzoyl peroxide is 4:1. The raw materials according to the above proportions are uniformly mixed in a high-speed mixer for 10 minutes without heating during the mixing process, and then extruded, drawn, cooled and granulated on an ordinary twin-screw extruder. The temperature range setting of the extruder: the barrel is between 110°C and 200°C, and the head and die are between 210°C and 220°C.
[0030] Take by weighing 70 parts of reactive polymer grafts, 30 parts of ethylene vinyl acetate with VA content of 28%, 170 parts of unmodified aluminum hydroxide (average particle diameter 1.3 μm), silicon dioxide (average particle diameter 20nm) ) 5 parts, 15 parts of PP...
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