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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Embodiment 1
[0017] Preparation of solid catalyst components
[0018] Under the protection of nitrogen, the stirring was started, and 40ml of decane, 7g of magnesium chloride and 30ml of isooctyl alcohol were successively added into the reactor, and then the temperature was slowly raised to 130°C, and the reaction was carried out at constant temperature for 2 hours. Then add 1.7 g of phthalic anhydride, continue the constant temperature reaction for 2 hours, stop stirring, and let it cool down to room temperature naturally for later use.
[0019] Add 200ml of titanium tetrachloride into the catalyst synthesis kettle fully replaced with nitrogen, lower the temperature to -22°C, drop the prepared magnesium chloride homogeneous solution at room temperature into it within 1 hour, and keep The temperature in the kettle is -22±1°C. After the dropwise addition is completed, add 3mg of silica gel with an average particle size of 1.5μm, keep the temperature for 1 hour, and slowly raise the temperat...
Embodiment 2
[0025] Catalyst components were prepared in the same manner as in Example 1, but when preparing the catalyst components, silica gel was added first, followed by magnesium chloride homogeneous solution, and the average particle diameter added was 1.5 μm of silica gel changed from 3 mg to 1 mg. Ti (weight %) is 2.55%. Polymerization was carried out in the same manner as in Example 1 using this catalyst component. The results are listed in Table 1.
Embodiment 3
[0027] Prepare the catalyst component with the same method as in Example 1, but when preparing the catalyst component, the silica gel with an average particle diameter of 1.5 μm added is changed from 3 mg to 4 mg, and polycarboxylate diisobutyl phthalate is changed to Di-n-butyl phthalate. Ti (weight %) is 2.86%. Polymerization was carried out in the same manner as in Example 1 using this catalyst component. The results are listed in Table 1.
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