Method for producing polyolefin-polyamide resin composition
a polyolefin and polyamide technology, applied in the field of manufacturing polyolefinpolyamide resin composition, can solve the problems of insufficient antioxidant with a low melting point, inability to long-time run, and extremely bad productivity, and achieve excellent productivity and long-time running
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example 1
[0042] Added into 100 weight parts of a low density polyethylene [(F522 available from Ube Industries, Ltd having a melting point of 110° C., MFR=5.0 (g / 10 min.)] as the component (a) are: 1.0 weight part of a γ-methacryloxy propyl trimethoxy silane [KBM503 available from Shin-etsu Silicone] as the component (c); 0.5 weight part of a pentaerythritol tetrakis[3-(3,5-di-t-butyl-4-hydroxyphenyl) propionate [Irganox 1010 available from Ciba Specialty Chemicals having a melting point of 110° C.] as the component (d); 0.5 weight part of a 4,4′-butylidene bis(3-methyl-6-t-butylphenol) [Sumilizer BBMS available from Sumitomo Chemical Industry having a melting point of 209° C.] as the component (e); and 0.025 weight part of a di-α-cumyl peroxide [Percumyl D40]. They are kneaded in a Banbury mixer for reaction at 170° C., and pelletized in a uniaxial extruder at 170° C. to produce a silane modified polyethylene. Into the produced silane modified polyethylene, 50 weight parts of nylon 6 [1030B...
example 2
[0043] As the component (e), 0.5 weight part of a 2-mercaptobenzoimidazole [Sumilizer MB available from Sumitomo Chemical Industry having a melting point of 285° C.] is employed instead of 4,4′-butylidene bis(3-methyl-6-t-butylphenol). As the component (b), 50 weight parts of nylon 66 [2020B available from Ube Industries, Ltd having a melting point of 255-265C.] is employed instead of nylon 6. The kneading and reacting temperature in the biaxial kneader is set at 300° C. With these exceptions, a polyolefin-polyamide resin composition is produced in the same manner as in Example 1. Amount of Discharge, Continuous Running Time, Uniformity of Strand Diameter, Cut of Strand, Generation of Gum, Scorch in Extruder, Yield, and Daily Production at the time are shown in Table 1.
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