A preparation method of a composite support for a propylene high temperature polymerization catalyst, a component of the propylene high temperature polymerization catalyst and the propylene high temperature polymerization catalyst
A technology of high-temperature polymerization and composite carrier, which is applied in the preparation of composite carrier for propylene high-temperature polymerization catalyst, components of propylene high-temperature polymerization catalyst and propylene high-temperature polymerization catalyst, and can solve problems such as difficult control of alcohol content, low isotacticity and complex process
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Embodiment 1
[0045] 1. Preparation of composite carrier
[0046] The silica gel carrier was first activated at 200°C for 1.5 hours, then the activation temperature was increased, and activated at 500°C for 4 hours; under nitrogen protection, 20.0 g of the activated silica carrier was added to 70 mL of toluene (toluene and silica The mass ratio of fluorene diether is 3:1), under stirring conditions, add 14.0g fluorene diether (the molar ratio of silicon dioxide and fluorene diether is 6:1), react at 15°C for 1 hour, evaporate the toluene solvent, and dry The treated silica gel carrier solid powder is obtained. Under the protection of nitrogen, 25.0 g of magnesium chloride and 42.9 mL of ethanol were added to the reactor (the molar ratio of ethanol to magnesium chloride was 2.8:1), and the temperature of the reactor was raised to 125 ° C until the magnesium chloride was completely melted.
[0047] Under the protection of nitrogen, add 5.0g of fluorene diether-treated silica gel carrier with...
Embodiment 2
[0053] 1. Preparation of composite carrier
[0054] Silica gel carrier pretreatment is the same as embodiment 1;
[0055] Under the protection of nitrogen, add 20.0g of magnesium chloride and 36.8mL of ethanol (the molar ratio of ethanol to magnesium chloride is 3.0:1) to the reactor, and raise the temperature of the reactor to 120°C until the magnesium chloride is completely melted.
[0056] Under the protection of nitrogen, add 5.0 g of the treated silica gel carrier with an average particle size of 20 μm to the reaction kettle for 30 minutes, and then add a mixed dispersant of 200 mL of liquid paraffin and 200 mL of methyl silicone oil preheated to 120 ° C into the reaction kettle to After stirring for 4 minutes at a speed of 800 rpm, the reaction mixture was transferred to a cooling kettle under the protection of nitrogen. The refrigerant in the cooling kettle was anhydrous hexane that had been precooled to -27°C in a sufficient amount. After stirring, cooling, MgCl is ob...
Embodiment 3
[0062] 1. Preparation of composite carrier
[0063] Silica gel carrier pretreatment is the same as embodiment 1;
[0064] Under nitrogen protection, add 20.0 g of magnesium chloride and 33.1 mL of ethanol (the molar ratio of ethanol to magnesium chloride is 2.7:1) to the reactor, and raise the temperature of the reactor to 115° C. until the magnesium chloride is completely melted.
[0065] Under the protection of nitrogen, add 10.0 g of the treated silica gel carrier with an average particle size of 20 μm to the reaction kettle for 30 minutes, then add the mixed dispersant of 200 mL of liquid paraffin and 200 mL of methyl silicone oil preheated to 115 ° C into the reaction kettle to After stirring for 4 minutes at a speed of 800 rpm, the reaction mixture was transferred to a cooling kettle under nitrogen protection. The refrigerant in the cooling kettle was anhydrous hexane that had been pre-cooled to -25°C in sufficient quantities. After stirring, cooling, MgCl is obtained a...
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