Resin composition, modifier, and resin composition including the modifier
A resin composition and a technology for the composition, applied in the field of resin compositions, can solve the problems of difficulty in separating each raw material and cannot be reused, and achieve the effects of excellent modification effect, excellent impact resistance and elongation at break
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Embodiment 1
[0086] As the resin composition (A), a resin composition having the following composition was used.
[0087] [Resin composition (A)]
[0088] 65% by weight of an ethylene-vinyl acetate copolymer (a1-25) (manufactured by Tosoh Corporation; trade name ULTRASEN 640) with a vinyl acetate content of 25% by weight and a melt mass flow rate of 3 g / 10 minutes
[0089] 10% by weight of ethylene-vinyl acetate copolymer (a1-50) (manufactured by LANXESS Co., Ltd.; trade name Levapren 500) having a vinyl acetate content of 50% by weight and a melt mass flow rate of 3 g / 10 minutes
[0090] 25% by weight of an ethylene-acrylic acid copolymer (a2-9) (manufactured by SK Global Chemicals; trade name SK Primacor 5980I) with an acrylic acid content of 9 mol% and a melt mass flow rate of 300 g / 10 minutes
[0091] The above resin composition was dry-blended, and using a twin-screw extruder (manufactured by TECHNOVEL; trade name ULTnano25TW) with a screw diameter of 25 mm, melted and kneaded under ...
Embodiment 2
[0100] As the thermoplastic resin (B), a thermoplastic resin composition having the following composition was used.
[0101] [Composition of thermoplastic resin (B)]
[0102] 70% by weight of low-density polyethylene (B-1) with a melt mass flow rate of 3 g / 10 minutes and a melting point of 111° C. (manufactured by Tosoh Corporation, trade name PETROSEN 205)
[0103] 30% by weight of nylon 6 (B-5) having a melting point of 220° C. (manufactured by Ube Industries, Ltd.; trade name UBE NYLON1022D)
[0104] 80% by weight of the thermoplastic resin (B) composition was dry-blended with 20% by weight of the resin composition (A) described in Example 1, and a twin-screw extruder (manufactured by TECHNOVEL; trade name ULTnano25TW) with a screw diameter of 25 mm was used. , melted and kneaded under the conditions of a resin temperature of 230° C. and a screw rotation speed of 300 rpm to obtain a composition.
[0105] The obtained composition was molded at a pressure of 10 MPa, a heati...
Embodiment 3
[0108] As the thermoplastic resin (B), a thermoplastic resin composition having the following composition was used.
[0109] [Composition of thermoplastic resin (B)]
[0110] 70% by weight of low-density polyethylene (B-1) with a melt mass flow rate of 3 g / 10 minutes and a melting point of 111° C. (manufactured by Tosoh Corporation, trade name PETROSEN 205)
[0111] 30% by weight of polyethylene terephthalate (B-6) (manufactured by UNITIKA Co., Ltd.; MA-2103) having a melting point of 255° C.
[0112] The thermoplastic resin (B) composition was dry-blended, and melted and kneaded at a resin temperature of 270° C. and a screw speed of 150 rpm using a twin-screw extruder (manufactured by TECHNOVEL; trade name ULTnano25TW) with a screw diameter of 25 mm to obtain a thermoplastic resin. Pellets of resin (B).
[0113] 80% by weight of the obtained thermoplastic resin (B) was dry-blended with 20% by weight of the resin composition (A) described in Example 1, and a twin-screw extru...
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