Catalyst component for ethylene polymerization and catalyst
An ethylene polymerization and catalyst technology, which is applied in the field of olefin polymerization, can solve the problems of waste, stickiness, and difficult catalyst preparation, and achieves the effects of improving particle shape, reducing the addition amount, and improving the sensitivity of hydrogen
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Embodiment 1
[0030] (1) Preparation of catalyst components: In the reactor fully replaced by high-purity nitrogen, add 6.0g magnesium dichloride, toluene 80ml, epichlorohydrin 6.0ml, tributyl phosphate 8.0ml, 2-chloroethanol in sequence 4.0ml, 2.0ml ethanol, heated to 70°C with stirring, and reacted at 70°C for 1 hour when the solid was completely dissolved to form a uniform solution. Cool down to 30°C, add 4.8ml of diethylaluminum chloride with a concentration of 2.2M dropwise, and maintain the reaction at 30°C for 1 hour. The system was cooled to -5°C, 40ml of titanium tetrachloride was slowly added dropwise, and then 5.0ml of ethyl orthosilicate was added to react for 1 hour. Slowly heat up to 80°C and react for 2 hours. Stop stirring, let it stand, the suspension will quickly separate into layers, remove the upper clear layer, wash twice with toluene, wash four times with hexane, and blow dry with high-purity nitrogen to obtain a solid catalyst component with good fluidity and narrow ...
Embodiment 2
[0034] (1) The synthesis of the catalyst is the same as in Example 1. The consumption of 2-chloroethanol is changed from 4.0ml to 3.0ml, and the consumption of ethanol is changed from 2.0ml to 3.0ml.
[0035] (2) Ethylene polymerization is with embodiment 1. Catalyst composition and polymerization results are shown in Table 1 and Table 2.
Embodiment 3
[0037] (1) The synthesis of the catalyst is the same as in Example 1. The consumption of 2-chloroethanol is changed from 4.0ml to 2.0ml, and the consumption of ethanol is changed from 2.0ml to 1.0ml.
[0038] (2) Ethylene polymerization is with embodiment 1. Catalyst composition and polymerization results are shown in Table 1 and Table 2.
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