Random copolymerization polypropylene, preparation method thereof, polypropylene cast film containing random copolymerization polypropylene and application of polypropylene cast film
A technology of polypropylene casting and random copolymerization, which is applied in the field of random copolymerization polypropylene and its preparation, and random copolymerization polypropylene cast film, which can solve the problems of poor quality, large gap and poor comprehensive performance of domestic products. problems, to achieve the effect of increasing melt flow rate, improving structure, and balancing rigidity and toughness
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[0027] First, the present invention provides a method for preparing random copolymerized polypropylene, comprising the following steps:
[0028] Under the combined action of the main catalyst and the co-catalyst, S1 propylene undergoes a prepolymerization reaction in the prepolymerization reactor to obtain a propylene prepolymer;
[0029] The first polymerization reaction of S2 propylene prepolymer and fresh propylene, hexene and hydrogen occurs in the first loop reactor to obtain the first polymerization reaction product;
[0030] S3 the first polymerization reaction product and fresh propylene, hexene and hydrogen have the second polymerization reaction in the second loop reactor to obtain random copolymerized polypropylene;
[0031] The main catalyst is a metallocene catalyst, and the metallocene catalyst includes a carrier and a metallocene component supported on the carrier; the carrier includes silica gel, and the metallocene component includes zirconocene dichloride, me...
Embodiment 1
[0049] (1) Preparation of random copolymerized polypropylene
[0050] ① Under the combined action of the main catalyst and the co-catalyst, propylene undergoes a pre-polymerization reaction in a pre-polymerization reactor to obtain a pre-polymerization reaction product.
[0051] 2. The prepolymerization reaction product and fresh propylene, hexene and hydrogen enter the first loop reactor to continue the polymerization reaction to obtain the first polymerization reaction product. The hydrogen concentration of the first loop reactor is controlled to be 800 ppm, and the reaction temperature is 80 ° C , the reaction pressure is 4.5MPa, and the hexene / propylene is 0.4wt.
[0052]3. The first polymerization product and fresh propylene, hexene and hydrogen enter the second loop reactor and continue to polymerize to obtain the second polymerization product, and the hydrogen concentration of the control second loop reactor is 800ppm, and the reaction temperature is 80 ℃ , the reactio...
Embodiment 2
[0061] The difference between this embodiment and Embodiment 1 is that,
[0062] In the first polymerization reaction, the hydrogen concentration of the first loop reactor was 850 ppm, and the reaction pressure was 4.5 MPa; in the second polymerization reaction, the hydrogen concentration of the second loop reactor was 850 ppm, and the reaction pressure was 4.5 MPa.
[0063] The melt flow rate of the random copolymerized polypropylene obtained using the above-mentioned process parameters was 6.2 g / 10min.
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