Ball shape catalyst for ethylene polymerization and preparation process thereof
An ethylene polymerization and catalyst technology, applied in the field of spherical Ziegler-Natta catalyst and its preparation, can solve the problems of poor fluidity, wide particle size distribution, high content of fine powder, etc., and achieve hydrogen sensitivity and excellent copolymerization performance , Conducive to industrial production, the effect of high polymerization activity
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Embodiment 1
[0022] Preparation of solid catalyst components
[0023] Under nitrogen protection, start stirring, add 54ml of white oil, 70ml of methyl silicone oil, 10g of magnesium chloride, and 17ml of ethanol to the reaction kettle in sequence, then slowly raise the temperature to 130°C, and react at a constant temperature under a pressure of 0.2MPa for 3 hours to obtain a homogeneous solution of magnesium chloride. Open the emulsifier, keep the reactor pressure at 0.05MPa, transfer the obtained magnesium chloride homogeneous solution to the 1000ml hexane solution that has been pre-cooled to -22°C through the emulsifier, keep stirring at low temperature for 1 hour, and then naturally heat up to At room temperature, the liquid was pressed out, washed with hexane four times, 100ml each time, and then dried with nitrogen at 60°C to obtain a magnesium chloride spherical carrier. The molar ratio of magnesium alkoxide was 2.47 for sampling analysis.
[0024] Transfer the obtained magnesium ch...
Embodiment 2
[0032] The catalyst component was prepared in the same manner as in Example 1, but when preparing the catalyst component, the amount of silicon tetrachloride was changed from 35ml to 50ml. Ti (weight%) was 4.61%. Polymerization was carried out in the same manner as in Example 1 using this catalyst component. The results are listed in Table 1 and Table 2.
Embodiment 3
[0034] The catalyst component was prepared in the same manner as in Example 1, but when preparing the catalyst component, the amount of silicon tetrachloride was changed from 35ml to 17ml. Ti (% by weight) was 5.11%. Polymerization was carried out in the same manner as in Example 1 using this catalyst component. The results are listed in Table 1 and Table 2.
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