A kind of catalyst component and catalyst for ethylene polymerization
An ethylene polymerization and catalyst technology, applied in the field of olefin polymerization, can solve the problems of troublesome waste liquid treatment, difficult stability control, unsatisfactory bulk density of catalyst system, etc. good effect
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Embodiment 1
[0030] (1) Preparation of catalyst components
[0031] In the reactor fully replaced by high-purity nitrogen, 4.5g of magnesium dichloride, 120ml of toluene, 10.0ml of epichlorohydrin, 10.0ml of 2-ethylhexanol, and 3.0ml of ethyl silicate were successively added, and the temperature was raised to 100°C, when the solid is completely dissolved to form a uniform solution, react at 100°C for 3 hours, then add 0.01 g of hydroxypropyl-α-cyclodextrin and continue the reaction for 1 hour. Cool the reaction system to -5°C, slowly add 25ml of titanium tetrachloride dropwise, keep the temperature constant for 0.5 hours, then slowly raise the temperature to 85°C, and react for 2 hours. Then stop stirring, let it stand, the suspension is quickly separated into layers, the supernatant is extracted, washed four times with hexane, and dried with high-purity nitrogen to obtain a solid catalyst component with good fluidity.
[0032] (2) Ethylene polymerization
[0033] A stainless steel react...
Embodiment 2
[0035] (1) The synthesis of the catalyst was the same as in Example 1, except that 12.5 ml of epichlorohydrin, 10.0 ml of 2-ethylhexanol, and 0.015 g of hydroxypropyl-α-cyclodextrin were used.
[0036] (2) Ethylene polymerization is with embodiment 1. The aggregation results are shown in Table 1.
Embodiment 3
[0038] (1) Except that the amount of epichlorohydrin is 10.0ml, the amount of 2-ethylhexanol is 5.0ml, the amount of hydroxypropyl-α-cyclodextrin is 0.010g, and the dissolution temperature is increased to 105°C, the synthesis of the catalyst is the same as the implementation example 1.
[0039] (2) Ethylene polymerization is with embodiment 1. The aggregation results are shown in Table 1.
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