Polymer membrane, and preparation method thereof
A technology of polymer film and polypropylene composition, applied in the production of bulk chemicals, etc., can solve the problems of poor rigidity and stiffness, transparency and impact resistance of polypropylene film, etc., and achieve high impact resistance , Simplify the process of selection and processing, and the effect of high transparency
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[0029] According to a preferred embodiment of the present invention, the polypropylene composition is prepared by continuous polymerization in the presence of a Ziegler-Natta catalyst with high stereoselectivity. The continuous polymerization method means that the preparation process includes at least two sequential steps, wherein component (a) (i.e. crystalline polypropylene A) and component (b) (i.e. ethylene-propylene elastic copolymer B) are each in It is prepared in a separate step and, in addition to the first step, the latter step is carried out in the presence of the polymer formed in the previous step and the catalyst used in the previous step.
[0030] In the preferred case above, since the polypropylene composition is prepared using a Ziegler-Natta catalyst with high stereoselectivity, the molecular weight distribution of the polypropylene composition and the molecular weight distribution of its component (a) are greater than 4 , preferably greater than 4.5, more pr...
Embodiment 1
[0088] (1) Preparation of polypropylene composition
[0089] The polymerization reaction is carried out on the above-mentioned horizontal gas-phase polypropylene pilot plant, and the reaction is carried out according to the above-mentioned method. The external electron donor used in the polymerization reaction is diisobutyldimethoxysilane, the first reactor is used to prepare component (a) by homopolymerization of propylene, the polymerization temperature is 66°C, the reaction pressure is 2.3MPa, and the residence time is 90 minutes . The second reactor is used for propylene copolymerization to prepare component (b). Ethylene and propylene are added into the reactor. The polymerization temperature is 66° C., the reaction pressure is 2.2 MPa, and the residence time is 60 minutes. The polymer obtained by the reaction is subjected to degassing and wet nitrogen deactivation treatment to obtain a polypropylene composition. The reaction conditions and product properties are shown ...
Embodiment 2
[0094] (1) Preparation of polypropylene composition
[0095] The polymerization reaction is carried out on the above-mentioned horizontal gas-phase polypropylene pilot plant, and the reaction is carried out according to the above-mentioned method. The external electron donor used in the polymerization reaction is diisopropyldimethoxysilane, the first reactor is used to prepare component (a) by homopolymerization of propylene, the polymerization temperature is 66°C, the reaction pressure is 2.3MPa, and the residence time is 90 minutes . The second reactor is used for propylene copolymerization to prepare component (b). Ethylene and propylene are added into the reactor. The polymerization temperature is 66° C., the reaction pressure is 2.2 MPa, and the residence time is about 60 minutes. The polymer obtained by the reaction is subjected to degassing and wet nitrogen deactivation treatment to obtain a polypropylene composition. The reaction conditions and product properties are...
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