Olefin polymerization catalyst and preparation method thereof and olefin polymerization method
A technology of olefin polymerization and catalyst, which is applied in the field of olefin polymerization, can solve the problems of high apparent density, high catalyst production cost, complex synthesis and purification process of diol ester compounds, etc., and achieve low production cost, high olefin polymerization activity, high The effect of catalytic activity
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[0019] The preparation method of the olefin polymerization catalyst of the present invention comprises: (1) contacting a magnesium compound, an organic epoxy compound, an organic phosphorus compound and an internal electron donor compound in a solvent to form a homogeneous solution; (2) in the presence of a precipitation aid , the homogeneous solution was contacted with a titanium compound to obtain a solid precipitate as the catalyst.
[0020] According to the present invention, although the purpose of the present invention can be achieved as long as the internal electron donor is introduced in step (1), the inventors found in the preparation process that by properly controlling the amount of the internal electron donor compound in step (1) , the activity of the synthesized catalyst can be higher, wherein, relative to each mole of magnesium element, the amount of the internal electron donor compound is preferably 0.005-15 moles, more preferably 0.06-10 moles.
[0021] The inv...
Embodiment 1
[0060] In the atmospheric pressure reactor that has been repeatedly replaced by high-purity nitrogen, add 4.8 grams of anhydrous magnesium chloride, 70 milliliters of toluene, 8.0 milliliters of epichlorohydrin, 12.5 milliliters of tributyl phosphate, and 0.5 milliliters of di-n-butyl phthalate (DNBP), at a temperature of 50°C, reacted for 2 hours, added 1.4 grams of phthalic anhydride and 55 milliliters of toluene, reacted for one hour, cooled to -28°C, added dropwise 56 milliliters of titanium tetrachloride (drop acceleration 5 ml / min), the temperature was raised to 85°C (the heating rate was 5°C / min), 0.6 ml of di-n-butyl phthalate (DNBP) was added, the temperature was maintained for one hour, filtered, the solid was washed twice with toluene, and then Add 48 ml of titanium tetrachloride and 72 ml of toluene, keep the temperature at 110°C for 0.5 hours, add 48 ml of titanium tetrachloride and 72 ml of toluene after filtering, and treat it once at 110°C for 0.5 hours, then tr...
experiment Embodiment 1
[0062] After 5 liters of stainless steel autoclaves were fully replaced with nitrogen, 5 milliliters of concentrations were added to be a hexane solution of 0.5 mol / liter of triethylaluminum and 1 milliliter of concentrations to be 1 mol / liter of methylcyclohexyldimethoxysilane ( CMMS) hexane solution and 10 mg of catalyst prepared in Example 1, then add 10 milliliters of hexane to flush the feed line, then add 1 liter (under standard state) hydrogen, and 2 liters of refined propylene, and heat up to 70 ° C. Polymerization was carried out at temperature for 1 hour. After the reaction, the temperature of the reactor was lowered and the stirring was stopped to discharge the reaction product to obtain an olefin polymer. See Table 1 for details of the results.
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