Propene polymer and preparation method and application thereof
A technology for polymerizing propylene polymers and olefins, applied in the field of propylene polymers and their preparation, can solve problems such as film tearing, hindering the diffusion of polymerized monomers, adverse effects on production efficiency, etc., and achieve the effect of ensuring the production process
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[0016] The present invention provides a method for preparing propylene polymer. The method comprises in a gas phase polymerization reactor, under the conditions of olefin gas phase polymerization, propylene, ethylene and C are selected from 4 -C 8 The α-olefin is in contact with the olefin polymerization catalyst system.
[0017] In the present invention, the propylene polymer refers to a combination of propylene, ethylene and C 4 -C 8 A random copolymer formed by copolymerization of the α-olefin of, wherein the α-olefin may be one α-olefin or two or more α-olefins.
[0018] According to the method of the present invention, the olefin polymerization catalyst system can be various catalyst systems commonly used in the art that can catalyze the organic stereopolymerization of propylene. Generally, the olefin polymerization catalyst system contains a solid component, an external electron donor compound and an organoaluminum compound, and the solid component contains a carrier and a tit...
Embodiment 1
[0088] This example is used to illustrate the propylene polymer and its preparation method according to the present invention.
[0089] The solid component of the catalyst (commercially available from Beijing Aoda Petrochemical Co., Ltd.) is screened so that the particle size of the solid component is 8-100 microns, and the particle size is the solid component in the range of 14-30 microns. The amount is 80% by volume. Such as figure 1 As shown, the particle size distribution curve of the obtained solid component is a unimodal distribution.
[0090] The solid component uses magnesium chloride as a carrier, wherein, based on the total amount of the solid component, the content of titanium in terms of elements is 2.5% by weight, and the content of di-n-butyl terephthalate is 10% by weight.
[0091] Add the catalyst solid component to 50m continuously at 0.63kg / h 3 In the continuous horizontal agitated bed gas phase reactor, use a pump to continuously add triethylaluminum, the amount o...
Embodiment 2
[0097] This example is used to illustrate the propylene polymer and its preparation method according to the present invention.
[0098] The propylene polymer was prepared by the same method as in Example 1, except that the pressure in the reactor was 2.4MPa, the temperature in the reactor was 60°C, and the hydrogen / propylene molar ratio (H 2 / C 3 ) Is 0.013.
[0099] The polymer obtained by the polymerization is in the form of granules without agglomeration, and there is no phenomenon of blocking the material discharge pipeline of the reactor when discharging. The composition and properties of the prepared propylene polymer are shown in Table 1.
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