Preparation process of catalyst for propylene polymerization
A technology of propylene polymerization and catalyst, which is applied in the field of preparation of Ziegler-Natta catalysts for propylene polymerization, which can solve the problems of fragility, poor particle size distribution and strength of catalyst particles, etc., and achieve the effect that is beneficial to industrial production
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[0016] Example 1
[0017] Preparation of solid catalyst components
[0018] Under the protection of nitrogen, the stirring is turned on, and 40 ml of decane, 7 g of magnesium chloride and 30 ml of isooctyl alcohol are sequentially added to the reaction kettle, and then the temperature is slowly raised to 130° C., and the reaction is kept constant for 2 hours. Then add 1.7 g of phthalic anhydride, continue constant temperature reaction for 2 hours, stop stirring, and naturally lower to room temperature for later use.
[0019] Add 200ml of titanium tetrachloride to the catalyst synthesis kettle fully replaced with nitrogen, cool to -22°C, drop the obtained homogeneous solution of magnesium chloride at room temperature into it within 1 hour, and keep it in the process of dropping The temperature in the kettle is at -22±1℃. After the addition is completed, add 3mg of silica gel with an average particle size of 1.5μm, keep the temperature for 1 hour, slowly increase the temperature to ...
Example Embodiment
[0024] Example 2
[0025] The catalyst component was prepared by the same method as in Example 1, but when preparing the catalyst component, silica gel was added first, followed by the homogeneous solution of magnesium chloride. The added silica gel with an average particle size of 1.5 μm was changed from 3 mg to 1 mg. Ti (wt%) is 2.55%. Using this catalyst component, polymerization was carried out in the same manner as in Example 1. The results are shown in Table 1.
Example Embodiment
[0026] Example 3
[0027] The catalyst component was prepared by the same method as in Example 1, but when preparing the catalyst component, the added silica gel with an average particle diameter of 1.5 μm was changed from 3 mg to 4 mg, and the polycarboxylate diisobutyl phthalate was changed to Di-n-butyl phthalate. Ti (% by weight) is 2.86%. Using this catalyst component, polymerization was carried out in the same manner as in Example 1. The results are shown in Table 1.
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