Method for preparing solid catalyst in olefin polymerization catalyst
A solid catalyst, a technology for olefin polymerization, which is applied in the field of solid catalysts in the preparation of olefin polymerization catalysts, and can solve the problems of high production cost, many production links, and product quality fluctuating easily.
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Embodiment 1
[0063] In a four-neck flask equipped with a stirrer, a reflux condenser is installed and a cumulative gas meter is connected to the reflux condenser. After the entire reaction device is fully replaced by nitrogen, 70.8ml of absolute ethanol and 1.26 grams of iodine are added to the container. , to dissolve it. Add 6 grams of metal magnesium inside, be warming up to the reflux temperature of ethanol under stirring condition, add dehydrated alcohol 47ml every 10 minutes from reflux, magnesium powder 6 grams, altogether 3 times. About 1 to 2 hours after the completion of the third addition, the liquid viscosity began to rise sharply (at this time, the reaction rate can be calculated to be about 85% by the amount of hydrogen generated), at this time, 259ml of toluene was added to the reaction system, and the reaction was continued until The whole reaction time is about 6 hours until no hydrogen gas is produced at the end of the reaction.
[0064] Then press filter the remaining l...
Embodiment 2
[0068] The basic preparation method is the same as in Example 1, except that the toluene added during the preparation of D is replaced with hexane. The solid catalyst component of gained is analyzed, and titanium content is 2.65 (wt)%, measures particle size distribution by laser particle size distribution instrument, D50: 32 microns, D10: 10 microns, D90: 65 microns, S ((D90-D10) / D50) was 1.72, and the particle sphericity L / W was 1.1. The catalyst activity is 44100 g polypropylene / g catalyst, and the polymer bulk density is 0.44 g / cm 3 .
Embodiment 3
[0070] The basic preparation method is the same as in Example 1, except that the reaction temperature during the preparation of D is controlled to 50°C. The solid catalyst component of gained is analyzed, and titanium content is 2.53 (wt)%, measures particle size distribution by laser particle size distribution instrument, D50: 25 microns, D10: 10 microns, D90: 55 microns, S ((D90-D10) / D50) was 1.8, and the particle sphericity L / W was 1.4. The catalyst activity is 35200 g polypropylene / g catalyst, and the polymer bulk density is 0.43 g / cm 3 .
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