Olefin polymerization catalyst ingredient, preparation method of the olefin polymerization catalyst ingredient, catalyst system, use of the catalyst system, and olefin polymerization method
A technology of olefin polymerization and catalyst, which is applied in the field of catalyst components for olefin polymerization and its preparation, catalyst system and application, and olefin polymerization. It can solve the problems of low catalytic activity and achieve high polymerization activity, high isotacticity, and high Yield effect
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[0030] According to the preparation method of the catalyst component for olefin polymerization provided by the present invention, the method may comprise the following steps:
[0031] (1) carrying out the first contact reaction with magnesium halide and alcohol compound in the presence of hydrocarbon solvent to form a homogeneous solution;
[0032] (2) In the presence of a precipitation aid, the homogeneous solution obtained in step (1) is subjected to a second contact reaction with a titanium compound to precipitate a solid precipitate to obtain a mixture containing a solid precipitate;
[0033] (3) carrying out the third contact reaction with the mixture obtained in step (2) and the internal electron donor compound to obtain a suspension;
[0034] Wherein, described co-separation agent comprises co-separation agent a and co-separation agent b, and described co-separation agent a is the glycol ester compound shown in formula (I),
[0035]
[0036] In formula (I), R 1 -R ...
Embodiment 1
[0096] (1) Preparation of catalyst components
[0097] In the reaction kettle that has been repeatedly replaced by high-purity nitrogen, 52.5mmol of anhydrous magnesium chloride, 328mmol of toluene, and 140mmol of 2-ethylhexanol were sequentially added, and the reaction was carried out for 3.0 hours at a stirring speed of 450rpm and a temperature of 110°C to obtain a stable and uniform 3,5-Heptanediol dibenzoate 0.8mmol (0.4ml) and dibutyl phthalate 2.6mmol (0.7ml) were added, stirred for 60 minutes, and cooled to room temperature.
[0098] Add 0.8mmol (0.4ml) of 3,5-heptanediol dibenzoate and 2.6mmol (0.7ml) of dibutyl phthalate to the homogeneous solution of the alcoholate that has been fully replaced with nitrogen, and the In a reactor with 1mol of titanium tetrachloride and 190mmol of toluene at -20°C, they are fully contacted at -20°C by stirring. After 5 hours, the temperature is raised to 110°C. During the heating process, solid precipitates are precipitated, and o-benz...
Embodiment 2
[0109] Only change 3,5-heptanediol dibenzoate 0.8mmol (0.4ml) and dibutyl phthalate 2.6mmol (0.7ml) in Example 1 to 1.6mmol and 1.05mmol respectively, The olefin polymerization catalyst component and polymer were prepared according to the method of Example 1. Table 1 shows the results of the amount of titanium used in terms of titanium element, the amount of precipitation aid a and the particle size distribution of the catalyst component during the preparation of the catalyst component. The polymerization activity of the catalyst system containing the catalyst components in the polymerization of propylene and the performance parameters of the polymers are shown in Table 2.
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